| Literature DB >> 24366046 |
Shalinee Naidoo, Ademola O Olaniran1.
Abstract
Since 1990, more than 1.8 billion people have gained access to potable water and improved sanitation worldwide. Whilst this represents a vital step towards improving global health and well-being, accelerated population growth coupled with rapid urbanization has further strained existing water supplies. Whilst South Africa aims at spending 0.5% of its GDP on improving sanitation, additional factors such as hydrological variability and growing agricultural needs have further increased dependence on this finite resource. Increasing pressure on existing wastewater treatment plants has led to the discharge of inadequately treated effluent, reinforcing the need to improve and adopt more stringent methods for monitoring discharged effluent and surrounding water sources. This review provides an overview of the relative efficiencies of the different steps involved in wastewater treatment as well as the commonly detected microbial indicators with their associated health implications. In addition, it highlights the need to enforce more stringent measures to ensure compliance of treated effluent quality to the existing guidelines.Entities:
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Year: 2013 PMID: 24366046 PMCID: PMC3924443 DOI: 10.3390/ijerph110100249
Source DB: PubMed Journal: Int J Environ Res Public Health ISSN: 1660-4601 Impact factor: 3.390
Figure 1Overview of treatment stages within a wastewater treatment plant. Adapted from EPA [16] and UNEP [17].
Overview of various secondary treatment options available.
| Treatment | Design criteria | Effluent quality | Advantages | Disadvantages | Ref. |
|---|---|---|---|---|---|
| 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) | [ | |
| 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 | Efficient BOD reduction; Nutrient reduction by aerobic and anaerobic | Significant space requirements; Efficiency is strongly affected by environmental factors; continuous maintenance required | [ | |
| 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 | [ | |
| oxygen supplied for initial sludge decomposition and provide agitation to promote flocculation; 85% sludge removed whilst 15% recirculated | BOD removal of | Production of high quality effluent; reasonable operational and maintenance costs | High capital costs; high energy consumption; regular monitoring required; back washing needed | [ | |
| 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 | 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 | [ | |
| 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 | [ | |
| 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 | 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 | [ | |
| 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 | [ | |||
| 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 | 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 | [ | |
Overview of treatment requirements for selected effluent discharges.
| 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 |
Note: Adapted from Wastewater Treatment Guidance Manuel—Syrian Lebanese Higher Council [32].
Microbial indicators and pathogenic organisms associated with waterborne diseases and common sources of contamination.
| Microorganisms | Diseases | Source | Numbers * | |
|---|---|---|---|---|
| Bacteria | Thyphoid fever | Human faeces | 0.2–8,000 | |
| Paratyphoid fever | Human faeces | |||
| Salmonellosis/gastroenteritis | Human/animal | |||
| Dysentery | Human faeces | 0.1–1,000 | ||
| Cholera | Human faeces | |||
| Gastroenteritis | Human/animal | |||
| Gastroenteritis | Human faeces | 106–107 | ||
| Gastroenteritis | Human/animal | 104–105 | ||
| 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 | ||
Note: * Numbers of infectious particles in raw sewage. Adapted from Ashbolt and Grabow et al. [45,46].
Currently used guidelines by the eThekwini Municipality (South Africa) for treated effluent being discharged into a receiving catchment.
| 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 |
Notes: Adapted from Government Gazette [61]. (A): Guidelines for effluent being discharged into any area other than that specified by B; (B): Guidelines for effluent being discharged into any catchment area/river or a tributary.