Treated Wastewater Effluent as a Source of Microbial Pollution of Surface Water Resources
Abstract
:1. Introduction
2. Sources of Domestic and Industrial Wastewater
3. Impact of Improperly Treated Wastewater Effluent
3.1. Effect on the Environment, Micro- and Macrofauna
3.2. Effect on Human Health
4. Overview of Steps Involved in Wastewater Treatment
4.1. Pretreatment
4.2. Primary Treatment
Treatment | Design criteria | Effluent quality | Advantages | Disadvantages | Ref. |
---|---|---|---|---|---|
WASTE STABILISATION PONDS | |||||
Anaerobic ponds | 2–5 m deep, pH usually below 6.5; less surface area; covered either by gravel, plants, steel, and plastic. Loaded at high rates to prevent inlet of any oxygen | BOD Removal of 60%–85% | Low cost, little excess sludge produced, Small pond volume needed; Low nutrient requirements; Low operating costs; no electricity required; Methane by-product | Requires more land; Long start-up period; Post treatment always required, can produce an unpleasant odour; Requires sludge removal more often; Operates optimally at warmer temperatures (>25 °C) | [10,19] |
Facultative ponds | Shallow—1–3 m deep; Length to breadth ratio should be a minimum of 2:1; lined with compact clay (minimum thickness 0.3 m) or polyethylene; formation of two layers—aerobic at surface and anaerobic at bottom | BOD removal of 70%–85% | Efficient BOD reduction; Nutrient reduction by aerobic and anaerobic bacterial processes as well as by surrounding plants; Natural aeration of the upper layer via movement of air; Low energy consumption | Significant space requirements; Efficiency is strongly affected by environmental factors; continuous maintenance required | [10] |
Maturation ponds (polishing ponds) | Shallow—0.9–1 m deep; allows for light penetration; completely aerobic; high pH and high concentration of dissolved oxygen due to algal activity; little biological stratification; size and number depends on required effluent pathogen concentration | Little BOD removal because most has been removed in previous stages | Removes excess nutrients and pathogens such as faecal coliforms | Small BOD removal; additional costs; additional land requirements | [10] |
SUSPENDED GROWTH SYSTEMS | |||||
Activated sludge | oxygen supplied for initial sludge decomposition and provide agitation to promote flocculation; 85% sludge removed whilst 15% recirculated | BOD removal of 90%–98% | Production of high quality effluent; reasonable operational and maintenance costs | High capital costs; high energy consumption; regular monitoring required; back washing needed | [20] |
Batch reactor | Equalization, biological treatment and secondary clarification are performed in a single reactor vessel using a timed control sequence; aeration may be provided by bubble diffusers/floating aerators | BOD removal of 89%–98% | Initial capital cost savings; all processes carried out in a single reactor vessel; timed cycles; requires limited land; equalization of processes | Higher level of sophistication and maintenance required as timing must be controlled; may discharge settled or floating sludge; clogging of aeration devices; requires oversized outfalls as effluent discharge is timed | [21,22] |
SUSPENDED GROWTH SYSTEMS | |||||
Aerated lagoons | Should be lined with clay or some natural source, 1.8–6 m depth, 10–30 day retention time, oxygen supplied by additional mechanical means | BOD removal of up to 95% | Low cost, low maintenance and energy requirements, can be well integrated into surrounding landscapes, reliable treatment even at high loads | Nutrient removal is less efficient due to short retention times | [23,24] |
FIXED FILM SYSTEMS | |||||
Conventional biofilters (trickling filters) | Bed with supportive media such as stones, plastic, wood; 0.9–2.4 m deep; oxygen supplied via natural flow of air | BOD Removal of between 80%–90% | Low land requirement Moderate level of skill required for operation and maintenance Suitable for small to medium communities | Accumulation of excess biomass will affect performance; high level of clogging thus regular backwashing is required; if suddenly shut down–anaerobic conditions result in reduced effluent quality; odour and snail problems | [25,26] |
Rotating biological contactors | High contact time; high effluent quality; resistant to shock hydraulic or organic loading; short contact periods; large active surface area; silent; low sludge production; easy transfer of oxygen from air | Continuous power supply required; oxygen may be a limiting substrate | [27] | ||
Biological aerated filters | Consists of a reactor container, media for supporting biofilm growth, influent distribution and effluent collection system;Optimal conditions—pH 6.5–7.5 with mixing; Media should be chemically stable, high surface area and low weight e.g., sunken clay, floating polystyrene beads | High nutrient removal (80%–100%) | Environmental factors such as pH, temperature will aid microbial growth; high removal efficiencies; can combine ammonia oxidation and solids removal in a single unit | Media may become clogged due to biomass growth and accumulation—may create resistance to air and flow of liquid; regular back washing is required to remove excess biomass and particles | [28,29] |
4.3. Secondary Treatment
4.4. Disinfection and Tertiary Treatment Processes
4.4.1. Disinfection
Chlorination
Ultraviolet Light
Ozonation
4.4.2. Tertiary Treatment
Nutrient Removal
Filtration
Activated Carbon
5. Methods of Effluent Disposal
Destination | Preliminary | Primary | Secondary | Tertiary |
---|---|---|---|---|
Irrigation | ||||
Produce Eaten Raw | YES | YES | YES | YES |
Other Produce | YES | YES | YES | NO |
GroundWater | YES | YES | YES | YES |
Surface Waters | YES | YES | YES | NO |
Sea Outfalls | YES | YES | YES | NO |
6. Commonly Detected Microbial Indicators in Treated Wastewater Effluent
Microorganisms | Diseases | Source | Numbers * | |
---|---|---|---|---|
Bacteria | Salmonella enterica subsp. enterica serovar Typhi | Thyphoid fever | Human faeces | 0.2–8,000 |
Salmonella enterica subsp. enterica serovar Paratyphi | Paratyphoid fever | Human faeces | ||
Salmonella enterica subsp. enterica serovar Enteritidis and Salmonella enterica subsp. enterica serovar Typhimurium | Salmonellosis/gastroenteritis | Human/animal | ||
Shigella sp. (Shigella dysenteriae, Shigella flexneri, Shigella boydii, Shigella sonnei) | Dysentery | Human faeces | 0.1–1,000 | |
Vibrio cholera | Cholera | Human faeces | ||
Vibrio parahaemolyticus | Gastroenteritis | Human/animal | ||
E. coli (E. coli O:148; O:157; O:124) | Gastroenteritis | Human faeces | 106–107 | |
Campylobacter sp. | Gastroenteritis | Human/animal | 104–105 | |
Clostridium perfringens | Human/animal | 6 × 104–8 × 104 | ||
Faecal streptococci | Human/animal | 4.7 × 103–4 × 105 | ||
Enterococci | Human/animal | |||
Viruses | Poliovirus | Poliomyelitis | Human faeces | 180–500,000 |
Rotavirus | Diahorrea, vomiting | Human faeces | 400–85,000 | |
Adenovirus | Gastroenteritis | Human faeces | ||
Norwalk virus | Diahorrea, vomiting | Human faeces | ||
Hepatitis A Virus | Hepatitis | Human faeces | ||
Protozoa | Cryptosporidium parvum | Diahorrea | 0.1–39 | |
Entamoeba histolytica | Amoeba dysentery | 0.4 | ||
Giardia lamblia cysts | Diahorrea | 12.5–20,000 |
6.1. Total and Faecal Coliforms
6.2. E. coli
6.3. Faecal Streptococci and Enterococci
6.4. Salmonella sp.
6.5. Shigella sp.
6.6. Vibrio sp.
6.7. Coliphages
6.7.1. Somatic Coliphages
6.7.2. Male Specific F-RNA Coliphages
6.7.3. Phages that Infect Bacteroides fragilis
7. Current Guidelines for Treated Effluent
Parameter | A | B |
---|---|---|
Colour/Odour/Taste | None | None |
pH | 5.5–9.5 | 5.5–7.5 |
Dissolved Oxygen (mg/L) | 75% saturation | 75% saturation |
Faecal Coliforms (CFU/100 mL) | 0 | 0 |
Temperature (°C) | 35 | 25 |
Chemical Oxygen Demand (mg/L) | 75 | 30 |
Electrical Conductivity (mS/m) | 75 | |
Total Suspended Solids (mg/L) | 90 | 10 |
Sodium Content (mg/L) | 90 | 50 |
Soap/Oil/Grease (mg/L) | 2.5 | None |
Residual Chlorine (mg/L) | 0.1 | 0 |
Free/Saline Ammonia (mg/L) | 1 | 1 |
Nitrate (mg/L) | None | 1.5 |
Orthophosphate (mg/L) | 1 | 1 |
8. Conclusions
Acknowledgments
Conflicts of Interest
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Naidoo, S.; Olaniran, A.O. Treated Wastewater Effluent as a Source of Microbial Pollution of Surface Water Resources. Int. J. Environ. Res. Public Health 2014, 11, 249-270. https://doi.org/10.3390/ijerph110100249
Naidoo S, Olaniran AO. Treated Wastewater Effluent as a Source of Microbial Pollution of Surface Water Resources. International Journal of Environmental Research and Public Health. 2014; 11(1):249-270. https://doi.org/10.3390/ijerph110100249
Chicago/Turabian StyleNaidoo, Shalinee, and Ademola O. Olaniran. 2014. "Treated Wastewater Effluent as a Source of Microbial Pollution of Surface Water Resources" International Journal of Environmental Research and Public Health 11, no. 1: 249-270. https://doi.org/10.3390/ijerph110100249
APA StyleNaidoo, S., & Olaniran, A. O. (2014). Treated Wastewater Effluent as a Source of Microbial Pollution of Surface Water Resources. International Journal of Environmental Research and Public Health, 11(1), 249-270. https://doi.org/10.3390/ijerph110100249