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
