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Chapter
Biological Wastewater Treatment
Olawale Theophilus Ogunwumi, Adeyemo Festus Adeniyi,
Mezie Chinazor Angus and Oche Sunday Oche
Abstract
Preventing environmental pollution by adequately treating the ever-increasing
volume of wastewater generated by the over 8.1 billion (UN 2024 projection) people
in the world, meeting governments’ often updated effluent quality standards as a
result of emerging contaminants in domestic and industrial wastewater, operating
wastewater treatment process to generate energy through methane production and
capture to save operating costs, and deploying a compact system to fit reducing
installation space are some of the daring challenges facing sustainable wastewater
treatment technologies today. Hence, there is a need for continued innovation and
development of treatment processes. The current chapter discussed advancements
in biological wastewater treatment technologies through the years with a focus on
reasons for improvements in technologies. Some of the reasons highlighted are capital
and operational costs, plant volumetric capacity, effluent quality, efficient nutrient
removal, biofouling and membrane clogging, treatment plant installation size, etc.
The chapter also discussed biochemical oxygen demand as a measure of water quality
for biological treatment systems, the role of genetically engineered microorganisms
in biological wastewater treatment, bioremediation as a biological treatment process,
treatment plant pilot-scale, and upgrade to full-scale.
Keywords: wastewater, biological treatment process, activated sludge, genetically
engineered microorganisms, biochemical oxygen demand, bioremediation, treatment
plant pilot-scale, treatment plant full-scale
1. Introduction
Wastewater (Figure 1), inevitably produced from domestic, industrial, agricultural, and commercial activities, mixtures from sewer and stormwater runoff [1], has
been described as used water generated from the use of freshwater, reclaimed/repossessed water, drinking water, raw and saline water in a variety of applications [2]
including dishwashing, laundry, showers [3], food and beverage production, boiler
cooling, textile manufacture, oil refining and gas production, mining activity, and
petrochemical production [4]. Wastewater usually contains chemical, physical, and
biological pollutants [5, 6] and its characteristics such as pH content, heavy metal
content, odor, and concentration of suspended solids, depending on its source [7, 8].
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Wastewater Treatment – Past and Future Perspectives
Figure 1.
Greywater, a domestic wastewater in a settling tank [1].
1.1 Sources and types of wastewater
Wastewater types can be described in terms of their source which influences the type of pollutants they contain. The common types of wastewater are
explained below.
• Domestic Wastewater or Sewage: This is used water from households, commercial, institutional, and public facilities in a municipal [9], transported through a
sewer [1]. It is produced from such activities as washing, bathing, cleaning, and
flushing. Variants of domestic wastewater include Blackwater (produced from
the combination of human waste and flushing water) and greywater (produced
from washing, bathing, etc.) [10]. The major pollutants in sewage are pathogens,
colloidal matter, grease and oils, nutrients, pharmaceuticals, soaps and detergents, food wastes, suspended solids, minerals [11], microplastics, microfibers,
etc. [12].
• Industrial Wastewater: This is the used water generated from the commercial
manufacture of a range of industrial products and commodities including
food and beverage, textile, shoe and leathery products, electronics and power,
metal finishing, petroleum and petrochemicals, mining minerals, and radioactive materials [4]. It is an aqueous discharge and byproduct of industrial
processes that is often generated from the cleaning activities associated with
these processes [4]. The characteristics, volume, biodegradability, recalcitrance to treatment, and quality of industrial wastewater vary depending on
its source industry [4]. Pollutants often found in industrial wastewater include
inorganic materials, heavy metals, organic materials, and nutrients including
nitrogen- and phosphorus-rich compounds, asbestos, pathogens, oils, and
chemicals [13].
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• Cooling Water: This wastewater which may cause thermal pollution, is generated
from boiler steam condensation and machinery temperature reduction activities [2].
• Leachate: Is the wastewater that is precipitated from water percolation through
solid wastes in a landfill or dumpsite [2, 14]. Leachate quality and indeed, its
pollutants depend on the type of landfill that generates it. For example, industrial waste landfills generate leachate [15] containing typical industrial pollutants
such as heavy metals, radioactive pollutants, and inorganic nutrients [2, 15].
• Surface Runoff: This is the wastewater flow from a mixture of stormwater,
rainwater, and snowmelt, which carries pollutants present on the ground along
the path of flow [2].
• Urban Runoff: This is the used water generated from urban landscape irrigation
and cleaning activities in cities and municipals [2].
• Return Flow: This is the wastewater flow containing pesticides, herbicide residues, animal wastes, dissolved nutrients and minerals, suspended soil, etc., from
agricultural activities [2].
1.2 The need for wastewater treatment
Wastewater treatment which involves the removal/reduction of pollutants in
wastewater [15], is often considered a form of water use as it is interconnected with other
forms of water usage [16] and is necessary to preserve public health, prevent environmental degradation and ensure water security for the ever-growing global population
(Figure 2) as wastewater is known to cause diseases such as hepatitis, cholera, cancer,
reproductive defects, dysentery, and developmental disorder in humans and animals
and, can lead to oxygen depletion and biodiversity reduction in natural ecosystems [18].
Figure 2.
United Nations projected data for world population from 2024 up to 2100 [17].
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Wastewater Treatment – Past and Future Perspectives
Some of the major reasons for treating wastewater are highlighted in the following
section.
• Public Health: Untreated wastewater discharged into water bodies in the environment can have devastating health effects on living things from water use due
to the presence of pollutants [16].
• Wildlife Ecosystem: Aquatic life and other creatures such as migratory birds are
negatively affected when untreated wastewater is discharged directly into their
habitat including oceans, rivers, marshes, beaches, and shorelines [16].
• Recreational and Tourism: Clean surface water can be a great recreational playground, sporting arena, and tourist attraction for most people where activities
such as fishing, swimming, boating, yachting, boat cruising, and picnicking can
be carried out [16]. Pollution by wastewater can prevent sporting activities and
recreation [16].
• Economic: Water pollution will affect the economy of a place when it affects
public health, prevents recreation and tourism, and affects fishing activities and
aquatic life population [19].
2. Basics of biological wastewater treatment
Biological wastewater treatment systems rely on beneficial bacteria and other
microbes to decompose organic pollutants in wastewater into simple substances like
carbon (IV) oxide (CO2) and water (H2O) and generate biological floc or sludge;
decomposition may occur aerobically or anaerobically [20]. These microbes might
be present in the water naturally or be deliberately introduced during treatment –
genetically engineered microbes (GEMs) [20]. Some of the concepts associated with
biological wastewater treatment are elaborated in the section below.
2.1 Aerobic vs. anaerobic processes
• Aerobic Processes: In aerobic biological wastewater treatment, bacteria decompose organic pollutants with the aid of oxygen [20]. Reducing organic chemicals
to simpler ones defines this process, which ultimately produces carbon dioxide,
water, and further microbial biomass [20].
• Anaerobic Processes: Contrarily, oxygen is not utilized during anaerobic biological treatment [20]. Anaerobes hasten the decomposition of organic compounds
by taking part in anaerobic digestion and related procedures [20]. Biogas is the
final byproduct of decomposing stabilized organic wastes and contains carbon
dioxide and methane [20].
2.2 The waste product: sewage sludge
Natural microbes decompose organic pollutants, resulting in the production of
sewage sludge as a byproduct [20, 21]. Sludge from sewage treatment plants, often
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called semi-solid waste, contains a broad range of organic and inorganic materials. The sludge is a reflection of the microbes’ leftovers, which include bacteria and
undigested organic waste [22].
2.2.1 Importance of sewage sludge
• Resource Recovery: Despite being regarded as waste, sewage sludge is a rich
supply of materials that can be utilized for resource recovery, which is why it is
important [23]. Due to its high organic content, anaerobic digestion offers great
promise as a feedstock for producing biogas, which might be used as a thermal
storage or energy source [23].
• Provision of Macro-nutrients: Sewage sludge contains numerous nutrients,
including nitrogen and phosphorus [23]. One way to boost crop yields
while decreasing reliance on synthetic fertilizers is to convert sewage into
fertilizer [23].
• Soil Enhancement and Land Use: Biosolids from treated sewage sludge can
improve soil quality in many ways [23]. This sustainable farming method
improves soil structure, water retention, and plant growth [23].
2.3 Carbon dioxide release: the final stage
Microorganisms digest organic matter and produce sewage sludge, thereby releasing CO2. The release of this gaseous byproduct marks the end of the biological treatment process, which reduces complex organic molecules to less harmful substances
with less impact on the environment [24].
2.4 Impact of biological wastewater treatment
• Greenhouse Gas Emissions: The CO2 is produced naturally by microbes,
but it does contribute to the overall quantity of gases released into the
atmosphere [24]. Wastewater treatment plants make great efforts to minimize
their environmental impact, but the fact that they nevertheless emit carbon
dioxide into the atmosphere highlights the critical need to discover solutions
to lessen this effect [24].
• Carbon Footprint Considerations: The carbon footprint must be considered
when evaluating the environmental friendliness of treatment plants [22, 24].
The case of biological wastewater treatment is a prime example of this. Common
elements of initiatives to decrease carbon emissions include the optimization
of treatment processes, the installation of energy-efficient technology, and the
investigation of alternative treatment options [23].
• Energy Generation: Energy generation (Table 1) will probably be a key focus in
the future of biological wastewater treatment. New methods of energy recovery
from wastewater treatment and sewage sludge processing, like enhanced anaerobic digestion and biogas capture, are being developed to reduce energy consumption and increase sustainability [23].
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Wastewater Treatment – Past and Future Perspectives
• Treatment Process Renewable Energy Integration: Wastewater treatment plants
are giving serious consideration to incorporating renewable energy sources like
solar and wind power [28]. In line with the larger objectives of renewable energy
adoption, these activities seek to lessen the treatment processes’ total impact on
the environment [29]. It reduces operating expenses by over 9% and increases
renewable energy consumption by over 5%, with thermoelectric ratio adjustment improving further [30].
2.5 Biological wastewater treatment and the circular economy: from waste to
valuable resource
The concept of circular economy now finds resonance with the future of biological
wastewater treatment. A change in perspective from seeing wastewater as a problem
to a valuable resource is evident in the growing interest in recovering resources from
sewage sludge, such as nutrients, and creating value-added products [31]. One example of the circular economy application is the concept of biorefinery, which involves
using wastewater treatment facilities to produce several goods through integrated
operations [31]. The goal of biorefinery strategies is to extract as much useful material
Energy (kWh/m3)
Constituent
Typical
concentrationsa
(mg/L)
Maximum
potential from
organic oxidationb
Required
to produce
fertilizing
elementsc
Thermal heat
available for heatpump extractiond
Organics (COD)
Total
500
Refractory
180
Suspended
80
0.31
Dissolved
100
0.39
Biodegradable
320
Suspended
175
0.67
Dissolved
145
0.56
Nitrogen
Organic
15
0.29
Ammonia
25
0.48
Phosphorus
8
0.02
Water
Totals
a
7.0
1.93
0.79
7.0
After Tchobanoglous and Burton [25].
Based on a theoretical 3.86 kWh energy production/kg COD oxidized to CO2 and H2O [26].
c
Based on production energy of 19.3 kWh/kg N by Haber-Bosch Process and 2.11 kWh/kg P after Gellings and
Parmenter [27].
d
Energy associated with a 6 °C change in water temperature through heat extraction.
Source: Ref. [28].
b
Table 1.
Domestic wastewater nutrient energy generation.
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as possible from wastewater, whether it is bioenergy or bio-based commodities. [31],
in their study, removed over 70% of nutrients and provided valuable biomolecules for
bioenergy production and nanoparticle synthesis.
3. Genetically engineered microorganisms (GEMs) for wastewater
treatment: unveiling opportunities and navigating challenges
An integral part of environmental engineering, wastewater treatment is undergoing a paradigm shift toward greater use of state-of-the-art technology. Along
these lines, GEM integration has been a promising new avenue for improving the
longevity and efficiency of wastewater treatment systems [32]. Taking a deep dive
into GEMs, this section explores their breadth, definition, and the complex relationship between the benefits and drawbacks of using them to treat wastewater.
Genetically modified microorganisms are the result of microbiology and genetic
engineering; these bacteria, fungi, and algae actively alter their genes to improve
performance [32]. With their ability to increase nutrient removal, tolerate harsh
environmental conditions, and augment pollutant degradation, GEMs provide
a molecular canvas for tackling the complex problems of modern wastewater
treatment [32].
3.1 Possible applications of GEMs to wastewater treatment
• Precision in Pollutant Degradation: GEMs enable pinpoint pollution degradation
in a new way. Through the intentional insertion of genes that produce specific
enzymes or metabolic pathways, these microbes can break down toxins more
thoroughly and efficiently [33].
• Adaptability to Diverse Environments: GEMs excel at adapting to demanding
environmental situations. Genes that provide resilience allow these microbes to
adapt to varied habitats with varying temperatures, pH, and salinity. GEMs are
useful wastewater treatment tools because they are versatile [32, 33].
• Enhancing Eutrophication and Nutrient Removal: GEMs can improve nutrient
uptake and removal from wastewater, especially nitrogen and phosphorus [33].
An essential element in preserving the ecological balance in receiving water bodies, this focused strategy addresses eutrophication concerns [33].
• Synergistic Bioenergy Production: In addition to removing pollutants, [34]
revealed that some GEMs can be engineered to produce biofuels while treating
wastewater, resulting in synergistic bioenergy production. Wastewater treatment plants may now serve as centers for resource recovery and environmental
responsibility thanks to this dual-purpose functioning, which is in line with
worldwide efforts toward sustainable energy generation [33].
• Customized Microbial Consortia: GEMs allow for the creation of customized microbial consortiums that are optimized for certain wastewater
compositions [33]. Through mutually beneficial relationships and metabolic
capacity complementarity, this microbial community orchestration can improve
treatment efficacy as a whole [33, 34].
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Wastewater Treatment – Past and Future Perspectives
3.2 Disadvantages of using GEMs to treat wastewater
• Protecting the Environment: Exploring Unknown Regions: Complex problems may arise with the discharge of GEMs into the natural environment. To
guarantee environmental safety, an understanding and careful approach to
GEM application are required due to concerns about unanticipated ecological
repercussions, such as possible changes to native ecosystems and gene transfer to
indigenous microbes [34].
• Understanding and Navigating Regulatory Frameworks: GEMs operate in a world
where regulations are complicated and frameworks vary worldwide. Science,
government agencies, and businesses must work together proactively to protect
public and environmental interests while also encouraging innovation [34].
• Long-Term Stability and Viability: GEMs encounter a complex problem when
used in real-world wastewater treatment scenarios. The effectiveness of GEMbased therapy systems over the long term might be affected by factors like predation, competition with local microorganisms, and changes in environmental
circumstances [34].
• Ethical Considerations – Harmonizing Development with Conscientious
Innovation: A rigorous evaluation of the limits of scientific intervention is
warranted in light of the ethical concerns raised by the intentional alteration of
microbial genomes [34]. If we want to see GEMs used responsibly and with social
acceptance in wastewater treatment, we need to set explicit ethical standards.
4. Bioremediation of domestic and industrial wastewater: application,
problems, and solutions
As a long-term, eco-friendly option for treating domestic and industrial
wastewater, bioremediation – a biological method of wastewater treatment and
water recovery – is gaining popularity. This section discusses the bioremediation
process, some specific examples, difficulties in its implementation, and possible
solutions.
4.1 Bioremediation for wastewater treatment
By harnessing the metabolic power of microbes to decompose and convert
contaminants into less dangerous forms, bioremediation (Figure 3) offers a comprehensive methodology for treating wastewater. This biological intervention has been
utilized in a wide variety of wastewater treatments, from simple domestic to intricate
industrial processes [35].
4.1.1 Bioremediation of domestic wastewater: examples
• Systems for Septic Tanks: One example of bioremediation in action is the use of
septic tank systems in residential areas [35]. Effective treatment of wastewater,
before discharge or additional treatment, is ensured by the microbial communities within septic tanks, which break down organic debris [35].
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Figure 3.
Bioremediation removes pollutants from onsite municipal wastewater using biochar through several processes
[35, 36].
• Realized Wetlands Design: Artificial wetlands purify wastewater with plants and
bacteria like natural wetlands. Microbial communities live in wetland system
roots and decompose, adsorb, and precipitate pollutants [35].
• Activated Sludge Systems: Activated sludge systems are widely employed in
wastewater treatment plants for municipal purposes. The aerobic bacteria in
activated sludge break down organic pollutants, cleaning the wastewater before
release or treatment [35].
4.1.2 Bioremediation of industrial wastewater: examples
• Textile Industry: Bioremediation has been deployed in the textile industry,
which utilizes a great deal of water and produces lots of contaminants. Microbial
consortia remove organic solvents, dyes, and other contaminants, a greener
treatment than conventional methods [35, 37].
• Petrochemical Industry: This industry struggles with complex effluent streams
containing hazardous chemicals and hydrocarbons. Bioaugmentation or the
introduction of certain microbes may improve hydrocarbon breakdown and
reduce the environmental impact of petrochemical wastewater [37].
• Food Processing Plants: Wastewater from these industries typically contains
significant levels of nutrients and organic materials. Bioremediation methods
like aerobic treatment and anaerobic digestion reduce environmental impact by
promoting organic breakdown [35].
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Wastewater Treatment – Past and Future Perspectives
4.2 Bioremediation challenges
• Pollutant Complexity: Wastewater pollutants are complex and variable, making
bioremediation difficult. Industrial effluents may require specialized microbial
communities and treatment methods to remove complex chemicals, heavy metals, and other contaminants [35].
• Variable Environmental Conditions: Temperature, pH, and nutrient availability affect bioremediation efficiency. Treatment results may not be repeatable due to changes in these factors that affect the efficiency of microbial
activity [37].
• Microbial Competition and Inhibition: In situations where microbial populations
are diverse, inhibition and competition among microbes within the treatment
system are possible [35]. The overall treatment effectiveness can be impacted
by imbalances caused by pollutants that promote the growth of particular
microbes [35].
• Slow Treatment Rates: Treatment rates in bioremediation techniques can be
slower than in chemical or physical methods, especially when dealing with stubborn chemicals [35]. In situations where quick and effective treatment is crucial,
this restriction could be a problem.
4.3 Innovative solutions and future directions
• Enhancing Biodegradation using Genetic Engineering: The use of genetic
engineering can boost microbes’ biodegradation capacities. To address some of
the difficulties caused by complicated wastewater compositions, microorganisms
that have been engineered (GEMs) with specific enzymes or metabolic pathways
can be used to target particular contaminants [37, 38].
• Developing Microbial Consortium for Bioaugmentation: To improve wastewater
treatment systems, specialized microbes are purposefully introduced, a process
known as bioaugmentation [30]. This process enables the optimization of
treatment systems tailoring microbial consortia, which in turn addresses specific
contaminants and enhances overall system resilience [30].
• Enhanced Control and Monitoring Technologies: Improvements in bioremediation process management are made possible by new developments in real-time
monitoring and control systems. Insights into microbial activities are obtained
by sensor technology and data analytics, enabling proactive modifications to
maximize treatment efficiency [30].
• Combined Treatment Approaches: Bioremediation, when combined with additional treatment methods like enhanced oxidation techniques or physicochemical
processes, provides a holistic and synergistic approach. Overcoming the limits
of individual treatments, this integrated strategy can boost overall treatment
performance [30].
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5. Biochemical oxygen demand (BOD) in wastewater treatment
Water quality evaluation and wastewater management are crucial to aquatic ecosystem sustainability and environmental engineering. Biochemical oxygen demand
(BOD) is a key indicator of biological wastewater treatment system performance and
organic matter pollution [39]. This section examines biochemical oxygen demand
(BOD), its importance to wastewater treatment, and its role as a key indicator of
water management strategy and sustainability.
5.1 BOD: an overview
Biochemical Oxygen Demand (BOD) can estimate how much oxygen bacteria
need to break down organic matter in water. BOD, which measures oxygen consumption by microbes breaking down complex organic compounds, originated in the
bacterial breakdown of organic substances [39]. Organic pollutants including sewage,
industrial effluents, and agricultural runoff raise wastewater BOD. Because microorganisms utilize dissolved oxygen, oxygen levels in treated effluent drop as organic
pollutants are broken down [39]. If oxygen loss is substantial, aquatic animals and the
environment can suffer [39].
5.2 Biological wastewater treatment efficiency by BOD measurement
• Treatment Efficiency by Procedure: The effectiveness of biological wastewater
treatment can be gauged by measuring BOD. Aerobic digestion, activated
sludge treatment, biofiltration, and other processes rely heavily on microorganisms to decompose organic contaminants in treatment facilities [39]. By
keeping tabs on BOD levels throughout treatment, we can learn how well these
biological mechanisms are working.
• Efficiency of Activated Sludge (aerobic) System: Microbial colonies in activated
sludge systems in municipal wastewater treatment facilities aerobically decompose organic pollutants [40]. We can measure BOD to assess how effectively
the system supports microbial growth. Operators can optimize conditions for
microbial activity and alter treatment parameters accordingly by tracking BOD
reductions through each stage of the process [40].
• Efficiency of Anaerobic Treatment: BOD readings are used as a measure of
the overall effectiveness of the anaerobic treatment procedures that purposely
reduce oxygen [39]. Anaerobic digestion produces biogas from organic matter.
Anaerobic reactors that monitor BOD keep methane-producing bacteria at ease
and remove organic contaminants effectively [39].
• Effectiveness of Constructed Wetlands: Using plants and bacteria in an analogous way that natural ecosystems work, artificial wetlands are utilized to treat
wastewater [40]. The biological breakdown of organic compounds by measuring
the BOD in the inflow and outflow of man-made wetland systems can provide
knowledge of the efficiency of these systems. The success of the treatment
process and microbial communities in eliminating contaminants from the water
is indicated by the decrease in BOD levels [40].
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5.3 BOD implications for water sustainability
• Effects on the Environment and the State of the Ecosystem: The environmental
impacts of water bodies with high BOD levels is substantial. The degradation of
aquatic environments by dissolved oxygen depletion impacts fish populations,
biodiversity, and ecological equilibrium. Sustainable water management requires
monitoring BOD levels to preserve healthy aquatic habitats [40].
• Regulatory Compliance and Water Quality Standards: As an important criterion
for wastewater discharge permits, BOD limitations are included in numerous
regulatory frameworks globally [39]. Businesses and cities must follow these
rules. To preserve water quality and lessen environmental impacts, sustainable
water management goes beyond what is required by regulations [39].
• BOD as a Pollution Source Indicator: One diagnostic tool for locating the origins
of water pollution is BOD analysis. The presence of organic contaminants can be
identified by analyzing variations in BOD profiles [39, 40]. This allows for the
implementation of targeted actions to reduce pollution where it is most prevalent. Proactively identifying and treating pollution causes is essential for sustainable water management [40].
• Using BOD in Representing Water Quality: To mimic the process of organic
pollutant breakdown in treatment systems, sophisticated water quality
models use BOD data [41]. The goal of these models is to help decision-makers
develop sustainable water management plans by projecting future BOD levels
under different scenarios [41]. Stakeholders can develop effective policies
and procedures by comprehending the possible effects of different elements on BOD.
5.4 Difficulty in measuring and interpreting BOD
• Changes with the Seasons and Other Factors: Temperature, nutrient variations,
and seasonal fluctuations are some of the elements that can influence the variability in BOD values [39]. To make educated decisions about water management
based on accurate interpretations, it is crucial to understand these variances.
• Non-specificity of BOD: Although BOD gives a general idea of how much organic
pollution there is, it does not break it down into kinds. Because of this lack of
specificity, it is difficult to identify which contaminants may necessitate tailored
treatment approaches [39, 41].
• Time and Resource Intensiveness: The time-consuming process of traditional
BOD determination methods requires samples to be incubated for many days.
Consistent monitoring is essential, but it might be difficult for smaller treatment
centers to allocate the necessary resources [39].
• Emerging Contaminants and BOD Limitations: The proliferation of new pollutants, such as medications and personal care items, poses problems that BOD
measurements cannot completely solve [39]. While these compounds might not
have a major impact on BOD, they can still harm aquatic ecosystems, which is
why we need other ways to measure their impact [39].
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5.5 Innovations and future directions in BOD analysis
• Sensor Technologies and Real-time Monitoring: Technological advancements in
sensors have made it possible to track BOD levels in real time. More adaptive and
responsive water management strategies are made possible by the continuous
data provided by online sensors, which allow for rapid responses to BOD changes
[40, 41].
• Molecular Methods and Biosensors: Rapid and specific BOD measurements are
made possible by biosensors and molecular methods, which target key microbial
markers [42]. These advancements in technology allow for more precise and
efficient BOD readings, which in turn shed light on the microbiological processes
at work in wastewater [42].
• Incorporating AI: Improving BOD prediction models is an area where artificial
intelligence (AI) shows enormous potential. Machine learning algorithms are
capable of sifting through massive datasets, finding patterns, and making
condition-specific predictions on BOD levels. Proactive decision-making in
water management is facilitated by this integration, which also improves the
precision of forecasts [40, 42].
6. Wastewater treatment plants and sewage sludge systems
If the ever-increasing global wastewater generation in different regions (in
billion m3) (Figure 4) and the large yearly per capital production (in m3/capita/
year) (Figure 5), are to be reused or discharged safely into the environment without
Figure 4.
Global regional wastewater generation projection to 2050 [43].
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Figure 5.
Yearly global regional wastewater generation per capita [43].
harmful, detrimental health effects, then wastewater must be treated to remove pollutants. This can be achieved in specialized process plants referred to as Wastewater
Treatment Plants (WWTPs).
Wastewater treatment plants are facilities that receive and treat domestic and
industrial wastewater by removing contaminants, such as coarse debris, grease
and oils, sand, organic and inorganic pollutants, and biodegradable materials, in
wastewater [44]. When these plants treat wastewater, they produce a mud-like, slurry
residue or sewage sludge as the byproduct of the treatment process due to biomass
activities of feeding on organic pollutants in the wastewater [44]; hence, treatment
plants are also sewage sludge systems.
The sludge produced during the wastewater treatment process contains pollutants
like heavy metals, pathogens like viruses, and a large mass of bacteria that can stabilize
organic matter in wastewater using aeration, hence the term “activated sludge” [44, 45].
The sludge also contains valuable nutrients like phosphorus and nitrogen that have important agricultural applications in being used as farmland improver and fertilizer [44].
6.1 Wastewater treatment plant operations
The wastewater treatment plant facility undergoes different processes/stages of
operation (Figure 6) to achieve an acceptable level of wastewater treatment suitable for reuse and discharge to the environment. These stages of operation, which
include preliminary treatment, primary, secondary, and tertiary treatments are
described below.
• Preliminary Treatment Operation: This is aimed at separating suspended, gross
solids such as large plastics, wood logs, fabric, and bottles, excess grease or oil,
and grit from raw wastewater from the sewer by channeling it through a trough
and moving screen or by cutting the large, foreign objects in small pieces with a
comminutor or a macerator and then removing them [44, 46].
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Figure 6.
Wastewater treatment processes [46].
• Primary Treatment Operation: This is a physicochemical wastewater treatment
operation that involves allowing relatively smaller suspended and settleable solids to precipitate out of the water by gravity settling and sedimentation, mechanical flocculation, or chemical coagulation [44, 46]. Here, further screening and
comminution of smaller solid materials from the preliminary operation can be
carried out (Figure 7) [47]. This operation is aimed at reducing the strength and
biochemical oxygen demand (BOD) of organic matter in wastewater, neutralizing acidic/alkaline wastewater by the addition of appropriate chemicals,
removing leftover grease and oil from preliminary treatment, and eliminating
volatile pollutants [44]. Also, wastewater equalization, which involves making
wastewater effluent homogenous by using mechanical paddles or aeration can be
carried out at this stage [46].
• Secondary Treatment Operation: The secondary treatment operation is a biological wastewater treatment that removes dissolved, organic matter or colloids in
wastewater when microorganisms consume organic pollutants in an aeration
tank (Figure 7), producing CO2 and water H2O in the process [46, 47]. This
operation, which may be an aerobic or anaerobic process, is aimed at removing
biodegradable materials and significantly reducing BOD, phenols, and oils in
wastewater [46].
• Tertiary Treatment Operation: This wastewater treatment operation is aimed
at removing non-biodegradable materials, minerals (such as the hydrated salts
of nitrogen and phosphorus known to cause eutrophication in surface water),
and heavy metals left in wastewater after the primary and secondary treatment
operations [46]. The tertiary treatment is necessary to provide final polished,
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Figure 7.
Primary and secondary operations of wastewater treatment [47].
high-standard effluent before reuse or discharge [48]. This treatment operation can be carried out through ion exchange, reverse osmosis, electrodialysis,
adsorption, evaporation, chlorination, and electrolytic recovery processes [46].
The main operations in tertiary treatment are filtering and backwash operations
(Figure 8) in which secondary effluent is allowed to flow through a filter bed of
anthracite, gravel, or sand, and, then passed through a trough containing alum to
Figure 8.
Tertiary operation of wastewater treatment [47].
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filter out finely suspended solids not previously removed [47, 49]. The backwash
operation involved removing entrained floc from the filters by allowing filtered
water to flow back through the filter media and be recycled [49]. Disinfection of
wastewater is achieved by chlorination where chlorine is dozed into the treated
effluent to kill any pathogen present and the effluent is dechlorinated to remove
excess concentration of injected chlorine in a final step before discharge to the
environment [49].
6.2 Biological wastewater treatment technologies
The secondary wastewater treatment process which uses microorganisms and
aeration to convert organic pollutants to simple substances, is a biological treatment
technology. The four (4) main forms of biological treatment technologies are the
Oxidation Pond, Trickling Filter, Rotating Biological Contactor, and Activated Sludge.
• Oxidation Pond: This large, usually shallow pond relies on the interaction
between bacteria, algae, and sunlight to treat wastewater. Also called stabilization ponds or lagoons, oxidation ponds, provide an arena for algal growth by
using sunlight’s energy, CO2, and inorganic compounds released by biomass
in the systems and, the algae in turn, release oxygen (O2) required by aerobic
bacteria to feed on organic matter in wastewater [47]. Oxidation pond designs
are made compact by installing external aerators (mechanical air diffusers) in
the pond [47]. Dredging, and gravity settling, filtration, or chemical treatment
are used to rid the pond of sludge deposits and leftover algae respectively [47].
• Trickling Filter: This biological wastewater treatment technology operates by
continuously spraying wastewater over a bed of stone in a tank and collecting
the trickling water at the bottom of the tank from where it is sent to a clarifying
tank [47]. Microorganisms on the surface of the stone bed consume organic matter in the wastewater as it flows thus, reducing its BOD and treating it [47]. The
circulating air passing through the spaces between the stones provides aeration
for the microbial activity of feeding on organic matter in the wastewater [47].
The performance of the trickling filter can be optimized by arranging two
or more filters in series and allowing treated effluent to recirculate through
them [47].
• Rotating Biological Contactor: In this technology, a layer of microbes growing
on a sequence of large, flat, plastic disks (in contact with the wastewater to be
treated) mounted on a rotating horizontal shaft, consumes the organic matter
in the water as each disk in turn, get exposed to atmospheric air due to shaft
rotation [47].
• Activated Sludge: Of the biological wastewater treatment technologies discussed so far, the activated sludge technology is the most globally applied and
effective [45]. A typical design consists of a primary aeration or mixing tank
and a secondary settling tank or clarifier for recycling returned sludge (RAS) for
a continuous process and increased efficiency [47]. Wastewater from primary
treatment is mixed with fresh sludge and RAS and, aeration from an external air
compressor is supplied to the mixture from porous diffusers at the bottom of the
mixing tank [47]. Aeration provides oxygen for microorganisms in the sludge
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which feed on organic materials in wastewater, reducing its BOD and forming
a mass of biological floc called Activated Sludge [47]. The treated effluent then
flows into the secondary settling tank where clear water is separated from the
activated sludge which is returned to the system (RAS) or removed as surplus
activated sludge (SAS) [47].
6.3 Developments in biological wastewater treatment process and emerging
technologies
Biological wastewater treatment technologies have evolved over the years as
industries and households continue to generate large volumes of wastewater and new
pollutants are discovered, prompting various national governments to update wastewater effluent discharge quality standards for the protection of human health and
the environment [47, 50]. Technologies have also been upgraded for sustainability via
energy production and waste resource recovery for a circular economy process [50].
The advancement in treatment technology has also helped to mitigate the effects of
future challenges such as increased wastewater generation from an increasing global
population, old and aging treatment facilities, limiting plant installation spaces, and
climate change, on the quantity of treated wastewater [47].
6.3.1 The stirred tank reactor technology
The activated sludge wastewater treatment technology is an ideal process for treating industrial wastewater in a stirred tank (agitated vessel) seeded with the biological
floc (sludge) and aeration at high pressure to supply adequate dissolved oxygen [50].
The stirred tank activated-sludge wastewater treatment technology is one of the oldest biological treatment processes first used at the Davyhulme Wastewater Treatment
Facility in the UK between 1912 and 1914 [45, 51, 52]. A typical system design usually
referred to as the conventional activated sludge (CAS), consisted of a single mixing
tank (agitated vessel), a settling tank (sedimentation tank), and a sludge recycle line
(RAS line) (Figure 9) [45, 51, 52]. This arrangement allows raw, influent wastewater
to be treated and effluent to be separated from the floc (activated sludge) which is
recycled or sent to sludge management as waste.
The capacity of the agitated vessel in an activated sludge process is usually large
and since oxygen dissolves very slowly in an aqueous solution, a major limitation of
the industrial application of the activated sludge process is the high cost of operation
arising from operating and maintaining high capacity air compressors [50]. Step
aeration technique can be used to improve the performance of the activated sludge
Figure 9.
Conventional activated sludge process [51].
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process whereby the process is modified by installing several small-sized, cascading
stirred tanks in sequence (The Bardenpho Scheme) instead of a single large tank;
the total volume of the small tanks being equal to the volume of the large tank [50].
This enhances higher BOD reduction, denitrification, and phosphorus elimination
from wastewater [50]. Higher process performance can also be achieved through a
sequential-parallel arrangement of the small tanks.
6.3.1.1 Design and performance characteristics of the activated sludge process
The stirred tank activated-sludge process is designed based on factors such as
characteristics of wastewater, government regulation, and treatment objectives [53].
The process design characteristics include:
• Dimension and capacity of the stirred (agitated) tank.
• Transfer system and oxygen requirement of the aeration process.
• Dimension and capacity of the settling tank.
• Design of the sludge return system.
• Design of the waste sludge withdrawal system.
• Mixing pattern of the wastewater and sludge (formation of mixed liquor suspended solid-MLSS).
The process performance of a stirred tank activated-sludge system can be hinged
upon various features some of which are:
• Contaminant Reduction: The activated sludge system can reduce up to 99%
BOD in secondary treatment and can achieve a high reduction of pathogens in
wastewater.
• Loading Rate: The system provides treatment flexibility by operating over a
range on hydraulic and organic loading rates.
• Resilience: The system is robust under varying operating conditions as it can
withstand different hydraulic and organic shock loads.
• Effluent Quality: Permissible discharge standards of wastewater effluent can be
achieved using the activated sludge system.
• Installation Space: The system requires a smaller installation space compared to
the system such as a stabilization pond [54].
• Nutrient Elimination: The system is ideal for high removal of nitrogen and
phosphorus. Also, the nitrification–denitrification process can be achieved by
upgrading with an anoxic chamber inside the aeration vessel [55].
Improvements on the stirred tank activated-sludge system include systems such as
the anaerobic-anoxic, oxygen ditch, and sequential batch reactor technologies.
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6.3.1.2 Anaerobic-anoxic-oxic (A2O) technology
This activated sludge technique is an improvement on the design of the CAS as
it allows easy elimination of phosphorus and nitrogen nutrients in wastewater. Its
arrangement (Figure 10) consists of an anoxic tank where a Modified LudzackEttinger (MLE) process takes place for denitrification, an anaerobic tank for
phosphorus removal by absorption, and an aerobic tank (oxic) for organic pollutant
decomposition [51, 56].
6.3.1.3 Oxidation ditch
This is an improvement over CAS where highly efficient rotating biological
contactors (RBCs) in the ditch (Figure 11) increase surface area and dissolved
oxygen available for microbial growth and activities, creating agitation and mixing
within the ditch as wastewater flows from a bar screen, leading to effective treatment
process [51].
6.3.1.4 Sequential batch reactor (SBR) technology
The SBR technology has the advantages of lower treatment area and cheaper
installation cost over the CAS because wastewater equalization, primary/secondary clarification, and microbial treatment take place in a single reactor unit (batch
operation) [57]. The SBR operation, commonly referred to as a “fill-and-draw”
process, first used a single unit, variable-volume, batch flow system for wastewater
Figure 10.
Typical arrangement of the A2O-activated sludge technology [51].
Figure 11.
The oxidation ditch process [51].
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treatment, but operational challenges forced an upgrade to a double unit, fixedvolume, continuous flow system with one unit used for aeration and the other for
settling [58].
Further upgrades to the SBR technology occurred in the 1950s and 1970s when
a continuous-feed batch treatment was incorporated in a variable-volume system
(by Pasveer and co-researchers) and in the USA and Australia, with the EPA’s grant;
the EPA’s publication of SBR design manual between 1982 and 1992 led to the global
application of the technology [58]. Today, the SBR process consists of a series of tank
units, each operated as a batch reactor. A typical treatment cycle goes through five (5)
stages such as fill, react, settle, draw, and idle (Figure 12).
Modifications of the SBR technology such as the sequencing batch biofilm reactor
(SBBR), and the anaerobic sequencing batch biofilm reactor (ASBBR) have recently
been developed to mitigate some challenges of the SBR technology including excessive sludge production and high sludge-volume index [57].
6.3.2 Membrane technology
The membrane bioreactor (MBR) technology (Figure 13), which is ideal for treating domestic and industrial wastewater, was developed in 1969 under the Dorr-Oliver
Scheme by Smith and co-researchers who combined biological treatment (in a bioreactor) with a membrane filtration process – ultrafiltration process (microfiltration is an
Figure 12.
Stages of the SBR process [58].
Figure 13.
The MBR process [59].
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alternative), instead of the settling tank used in activated sludge system [60]. While the
decomposition of organics occurs in the bioreactor, separation of floc from treated water
occurs on the membrane (with different pore sizes), this allowed for maximum sludge
separation from the treated water than in CAS [60]. Limitations such as membrane
fouling that causes clogging, and huge energy costs from membrane scouring, led to the
upgrade of the original MBR configuration in 1989 by Yamamoto and other researchers,
where a hollow fiber membrane and suction pump (rather than a pressure pump) were
placed in the bioreactor where the membrane is immersed [60]. The acceptability of the
MBR process increased since the 1990s mainly due to the advancement brought about
by the process upgrade (immersion configuration), which provided permeates of high
quality and reduced capital costs and clogging [60]. Future MBR process upgrades can
be achieved by expanding fiber membrane applications.
6.3.2.1 Design and performance characteristics of the MBR process
Some of the design characteristics of the MBR technology are elaborated in the
section below.
• Activated Sludge Process Design: Activated sludge process design is an integral
part of the MBR technology in combination with the membrane filtration
process. The design of the activated sludge process depends on microbial growth
considerations, oxygen supply, and dimension of the bioreactor [50].
• Membrane Material Selection: Polymer or ceramic material is selected for membrane material based on wastewater characteristics.
• Flux Rate of Membrane: Maintaining performance of membrane by balancing
the filtration rate.
• Hydraulic Configuration: Hydraulic mechanism design of MBR systems which
can be side-streamed or submerged.
• Energy Optimization: Energy optimization during filtration and aeration is a key
aspect of MBR operation.
• Cleaning System: The type of cleaning mechanism including air scouring or
backwashing should be considered during the design of the MBR system [61].
MBR process performance characteristics include:
• System Footprint: Since a separate settling tank is not required, the operation of
the MBR system has a smaller footprint (space) than CAS.
• High Energy Requirement: Membrane scouring process in MBR operation
increases the energy requirement for operation and is mitigated by developing
membrane with biological and chemical resistance, fouling control mechanisms,
and new configuration.
• Quality of Effluent: MBR operation produces non-potable effluent of high quality, which can be treated further for potable water recovery.
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• Process Fouling: organic matter from microbial cells is deposited on the membrane during operation. This can be mitigated by selecting new materials and
developing new configurations [62].
6.3.3 Biofilm technology
6.3.3.1 Moving-bed biofilm reactor (MBBR) technology
This technology was developed between 1988 and 1990 by Hallvard Odegaard [63]
due to the challenges of earlier wastewater treatment reactors including biofouling
(MBR), uneven biofilm distribution, and hydraulic instability (biofilm reactors) [64];
malodor pollution and expensive operational costs (trickling filters); mechanical failure,
high maintenance, and large area requirement (rotating biological contactor) [65]. In an
MBBR process (Figure 14), biofilm for wastewater treatment grows on movable carriers (biocarriers) in the aeration tank (oxic zone) and is separated from treated water in
the settling tank [65, 67]. These biocarriers come in different shapes, surface areas, and
configurations, and while the common configuration is a hollow cylinder, surface area
size is very crucial to biofilm formation – a large surface area provides intimate contact
for bacteria, wastewater, nutrients, and oxygen in the aeration tank [64, 65]. Operational
challenges of the original MBBR system such as inappropriate/slow biofilm growth
rate caused by increased solid retention time (SRT), high biofouling, and reduced mass
transfer [68], led to the development of a hybrid MBBR system– the moving-bed biofilm
membrane reactor (MBBMR), around the mid-1990s [63, 69, 70], which separates biofilm from treated water using a membrane instead of a settling tank [67]. This advanced
MBBR system had advantages such as low sludge generation, improved operational
efficiency, and reduced biofouling [68]. MBBR system’s performance can be evaluated
on factors such as biocarrier configuration and design, flexibility of filling fraction
(biocarrier size) according to system requirements, biofilm development (whether thick
or thin) based on the nature of biocarrier and which affects hydrodynamics of wastewater particles, uniform dissolved oxygen (DO) or aeration supply based on reactor
design [65], and hydraulic retention time [71]. Pilot-scale MBBR operations are essential
to assess full-scale process cost, scaling factor, feasibility, time, and unforeseen treatment results [72]. Some of the desirable qualities of a good biocarrier are light density,
Figure 14.
The MBBR process. WSS = Waste Solid Sludge [66].
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non-biodegradable, high resistance to abrasion, insolubility, microbial nontoxicity, and
high effective surface area [65, 73]. It is obvious that biocarriers are essential and very
critical to the effectiveness and performance of MBBR operations, future improvements
should focus on the configuration, geometry, and design of these biofilm carriers.
6.3.3.2 Design and performance characteristics of MBBR process
The MBBR design is an hybrid configuration of biofilter and activated sludge
processes for efficient wastewater treatment. The design characteristics are as follows.
• Hybridization Design: A free floating biofilter media for biomass concentration
is incorporated into the activated sludge system.
• Scalability: The MBBR technology is designed for easy scale-up and
modification.
• Biofilter Design: The configuration and design area of the biocarrier are important aspects of MBBR design.
• Biofilter Mixing: The process is designed for effective biocarrier mixing to
distribute biofilm evenly through the CAS system.
• Aeration Supply: The system supports adequate oxygen supply [65].
MBBR process performance can be affected by characteristics such as:
• Biofilter Surface Area: The MBBR process relies on biofilm formation on the
biofilter for wastewater treatment. This surface area affects biofilm growth as a
larger area enables large bacteria colonies.
• Nutrient Concentration: The process is ideal for high organic (carbonaceous) and
ammonia (nitrogenous) wastewater nutrient removal.
• Process Hydraulic Retention Time: The process supports high influent retention
time for effective treatment.
• Adequate Process Conditions: The MBBR process can support optimal temperature and pH conditions [65].
6.3.3.3 Integrated fixed-film activated sludge (IFAS) technology
The IFAS technology is a hybridization of the MBBR and CAS technologies, an
advancement over MBBR by incorporating suspended and attached growth systems [74]
and the most recently invented biological wastewater treatment process having been
developed around the early 2000s [75, 76]. This hybrid system involves adding a fixed
microbial growth media (MBBR technique) to an activated sludge (AS) tank (CAS
technique) to provide a biofilm growth surface and enhance nitrogen elimination by
the oxidation process, respectively [75, 76]. This technology (Figure 15) allows the
suspended-growth microorganisms of CAS and biofilm bacteria to be combined in a
single reactor unit, allowing two different kinds of microbes (aerobes and anaerobes)
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Figure 15.
The IFAS process. M = Stirrer motor [77].
to work in tandem; while the mixed liquor suspended solid (MLSS) biomass (aerobes)
decomposes organic wastewater load, the biofilm (anaerobes) sets up a strong nitrifying
bacteria to oxidize nitrogenous load [76]. The IFAS technology offers some advantages
over traditional MBBR systems including a larger surface area of media for biofilm
growth that provides higher efficiency in eliminating phosphorus and nitrogen, higher
biomass concentration, organic load, and treatment capacities, more energy efficiency,
and less capital cost [77]; although the movable MBBR system’s media prevents clogging,
promoting diverse bacteria growth, the system is also more compact, and resistant to
organic shock load [77]. Over CAS technology, the IFAS system’s advantage includes
complete nitrification, reduced footprint, longer solids retention time, enhanced
anthropogenic composite, and nutrient removal [74]. Pilot- and full-scale IFAS systems’
performance can evaluated on factors such as hydraulic retention time (HRT), solid
retention time (SRT), biocarrier media, media filling ratio, and dissolve oxygen concentration (DO) [74]. Recent upgrades to the IFAS process incorporated systems for energy
generation, methane production, and capturing [74].
6.3.3.4 Design and performance characteristics of the IFAS system
The IFAS system is mainly characterized by the design of a hybrid suspended and
attached growth process where a biofilm carrier surface is attached to the activated
sludge suspended-growth system to enhance treatment efficiency [78]. The performance
of the IFAS system is centered around its operational efficiency, removing above 93% of
chemical oxygen demand (COD) in industrial wastewater and, microbial synergy, where
suspended- and attached-growth microbes are involved in the treatment process [78].
6.3.3.5 Downflow stationary/fixed-film bioreactor (DSFF) technology
This technology (Figure 16), which has been in operation for several decades,
is ideal for treating and purifying industrial wastewater by allowing the downward
flow of the influent wastewater through a bed of biofilm, causing microorganisms to
break down organic matter in the wastewater [78]. This has the advantage of moving
wastewater by gravity rather than mechanical agitation, thereby reducing operational
costs and ensuring efficient dilution of waste matter in the reactor [78]. Some of the
limitations of the DSFF reactor include optimizing biofilter surface area, choosing an
appropriate material for film support, the effect of reactor height on its temperature
gradient, and wastewater load fluctuations [80].
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Figure 16.
Schematic diagram of a typical DSFF process [79].
The DSFF technology is an efficient biological treatment technology, and
researchers have continued to focus on its development. Future developmental
improvements are in the direction of improving biofilm media, developing novel
strategies for biofilm attachment, adopting liquid phase oxygen technology for system
aeration, and using alternative reactor configuration [81].
6.3.3.6 Design and performance characteristics of the DSFF system
The design characteristics of the DSFF system are as follows.
• Support Media: The system is designed to utilize a support medium including polymer beads, activated carbon particles, or silica granules, for bacteria
colonies [50].
• Wastewater Flow Pattern: The downward flow design of the DSFF system allows
the dilution of waste as it enters the system [80].
DSFF process performance can be associated with the following characteristics.
• Film Surface-to-Volume Ratio: Optimizing biofilter surface area to biofilm
volume is key to the efficient performance of the treatment process.
• Reactor Height and Process Temperature: High bioreactors may have the challenge of distributing substrate uniformly and temperature fluctuations throughout the height of the reactor.
• Biofilm Support Media: The performance of the DSFF system depends on the
type of support media selected for the process [50, 80].
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6.3.3.7 Packed-bed biofilm reactor (PBBR) technology
This system creates a biofilm for wastewater treatment by filling a packed-bed
bioreactor with supporting materials – usually cylindrical glass carriers (Figure 17), so
that microorganisms attached to the surfaces of these carriers metabolize pollutants in
wastewater [83] as they flow through the bed [81]. Recent applications of this technology
(a typical example is the trickle-bed biofilm reactor process) have combined biofilm
aggregate on carriers with membrane technology processes like ultrafiltration [50, 83].
Although the packed-bed biofilm wastewater treatment technology is an advanced treatment process suitable for industrial wastewater, it has limitations, some of which include
restriction of oxygen and wastewater nutrients from the bulk liquid to the biofilm,
reduced flowrates due to media clog by organic matter, biofilm detachment, channeling,
biofilm susceptibility and slow response to shock loads, and scale-up complexities [83].
6.3.3.8 Design and performance characteristics of the PBBR system
The design attributes of a PBBR process include reactor geometry and configuration, which accounts for the surface property, size, and shape of the bioreactor and
can allow maximum nutrient removal without accumulation; media configuration
including its surface property, shape, elasticity, size, mass, and absolute size; design
of wastewater loading pattern and media remover/cleaning mechanism [84]. PBBR
process efficiency is characterized by factors such as optimal biofilm thickness which
provides sufficient surface area for microbial activity without clogging, good quality
support media, appropriate hydraulic retention time, and adequate aeration through
the bulk liquid to the biofilm [84].
Figure 17.
The PBBR wastewater treatment process [82].
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6.3.3.9 Fluidized-bed biofilm reactor (FBBR) technology
This technology is a recent advancement in the biofilm wastewater treatment
process and operates by suspending support media (biocarriers) in the reactor
with the force of upward-flowing feed wastewater (Figure 18) [50]. The FBBR
process is applicable for industrial installations and large treatment facilities due
to its high fluid flowrates, usually higher than the smallest fluidization velocity
but lower than the biofilm aggregates terminal free velocities in the reactor; this
causes a suspension (fluidization) of the biofilm aggregates [50]. One advantage
of this process is that there is no channeling as biofilm aggregates are surrounded
by the wastewater, which improves intimate contact (between bacteria and wastewater organic pollutants) and reactor performance [50]. Also, the process can
handle higher wastewater throughput as a result of effective bacteria retention and
produces less sludge. Limitations of the FBBR technology include high operating
costs from keeping media fluidized by aeration, media fouling, limited nutrient
removal, biofilm detachment, scale-up complexities, and other than industrial
wastewater with high organic pollutants, it is inadequate for treating other types of
wastewater [50].
6.3.3.10 Design and performance characteristics of the FBBR system
A notable design characteristic of the FBBR system is its compact design, which
makes it suitable for isolated and localized wastewater treatment applications [86].
Figure 18.
The FBBR wastewater treatment process [85].
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Additionally, the diameter of the media and bioparticle, substrate penetration
depth, and internal/external mass transfer coefficients are other important design
attributes [86]. The process performance can be attributed to characteristics that
include efficient mixing and mass transfer, significantly high wastewater throughput
and up-flow velocity, optimal pH and temperature, media porosity, and surface area
(a balance between these can achieve efficient treatment), and pollutant loading rate
[86, 87].
The semi-fluidized-bed (SFBBR) and inverted fluidized-bed (IFBBR) biofilm
wastewater treatment processes are similar to the FBBR process as they both utilize
suspended media particles (fluidization) for microbial growth required for wastewater treatment, but while the particles are partially suspended in SFBBR, they are
expanded in IFBBR [85–87]. While the FBBR process focuses on biomass holdup
(concentration), the SFBBR process emphasizes efficient mass transfer and optimal
mixing, and the IFBBR process focuses on faster process startup [88]. The major
limitation of the SFBBR process is the limited biomass concentration (retention) in
the reactor while optimizing startup time, which is a major problem of the IFBBR
process [89].
6.3.3.11 The sludge blanket biofilm reactor (SBBR) technology
This technology utilizes sludge granules (microbial colonies) formed from bacterial
cells on support media (biofilm) and the accumulated biomass layer (sludge blanket) at
the bottom of the reactor for wastewater treatment [81]. Wastewater passes through the
sludge blanket and the biofilm simultaneously for enhanced treatment by suspended
growth and biofilm-based microbes, respectively. The SBBR treatment process is
similar in design to the up-flow anaerobic sludge blanket process (UASB) (Figure 19)
however in UASB, treatment is carried by the suspended-growth microorganisms and
Figure 19.
The UASB process has a similar design to the SBBR [90].
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this is done without the supply of oxygen [50, 81]. Some of the limitations of the SBBR
process include high operational costs from poor settling of solid pollutants in the
sludge blanket and high sludge production, high levels of toxic substance accumulations
with the blanket, and engineering design and operation challenges [91].
6.3.3.12 Design and performance characteristics of the SBBR system
The characteristics of SBBR design that contribute to its performance include the
reactor configuration, biofilm support media design material, configuration, etc.
Attributes such as optimal process pH and temperature, microbial interactions, and
sludge settling properties affect SBBR system performance [81, 91].
Bioreactor
Merits
Limitations
Stirred tank
Simple in construction and operation. Uses suspended
growth of microbes. Suitable for aerobic and
anaerobic processes.
Restricted to low capacities.
Trickle-bed
biofilm reactor
Use of attached growth of microbes. Low operating
cost due to down flow mode of operation. High
cell mass concentration in biofilm promotes rate of
bioconversion.
Mainly for aerobic BOD
removal. Low capacity
due to low feed flow rate
maintained.
Moving-bed
biofilm reactor
(slurry reactor)
Heterogeneous version of stirred tank. High
cell concentration in biofilm promotes rate of
bioconversion.
Capacity wise inferior to
column reactors, Biofilm
could get disturbed due to
high rate of agitation.
Fluidized-bed
biofilm reactor
Operates at high capacities, provides high degree
of bioconversion. Once fully fluidized, pressured
drop across the bed remains constant and does not
increase with increase in feed flow rate. Degree of
bioconversion increases with increase in feed flow rate
due to bed expansion.
Entrainment loss of particlebiofilm aggregates possible.
Operating cost higher than
trickle bed (packed bed).
Semifluidized bed
biofilm reactor
Higher degree of bioconversion (than fluidized
beds) at higher capacities and low reactor volume
requirement. Degree of bioconversion increases with
increase in feed flow rate, even if reactor volume is
kept constant.
Higher operating cost than
fluidized beds. Continuous,
circulating mode of
operation not possible.
Inverse fluidized
biofilm reactor
Low operating cost due to down flow mode of
operation. Larger-sized particles could be used.
Reasonably large degree of bioconversion.
Lower capacity than
fluidized/semifluidized
bed. Larger reactor volume
requirement.
DSFF bioreactor
Simple in construction and operation. No support
particles required. Low operating cost due to
downflow mode of operation. Multiple tubes/
columns could be used to increase capacity.
Presently restricted to
anaerobic operation. Large
reactor volume requirement
at high capacities.
UASB reactor
Simple in construction. No support particles used.
Provides substantially high degree of bioconversion at
distinctly high capacities and even with high-strength
feedstock.
Restricted to anaerobic
processes, employing
complex culture of microbes.
Enormously large startup
time.
Source: Ref. [50].
Table 2.
Comparison of stirred tank and biofilm biological wastewater treatment technologies.
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A comparison of the biological wastewater treatment technologies (especially the
stirred tank and biofilm technologies) discussed so far in this chapter is provided in
Table 2, including their merits and limitations. Other emerging biological wastewater
treatment technologies for sustainable water treatment and energy generation, some of
which do not incorporate the use of bacteria colonies, are phytoremediation, which uses
specific plant species to remove wastewater pollutants, and algal-based treatment, which
uses algal organisms to metabolize and remove wastewater pollutants; also, the microbial
electrochemical system (MES) generates electrical energy from microbial metabolic
activities during wastewater treatment [92–94]. These technologies have proven to lessen
the impact of wastewater treatment on the environment [92].
7. Conclusion and future perspectives
This chapter discussed the fundamentals of biological wastewater treatment as it
relates to the most commonly generated wastewater types – domestic and industrial
wastewater. Wastewater is treated to protect public health and wildlife ecosystems,
provide recreation and tourism, and increase economic prosperity using biochemical
oxygen demand (BOD) analysis as a metric for water quality and treatment effectiveness. Biological wastewater treatment is an eco-friendly process that relies on microorganisms to convert organic pollutants in wastewater to simple substances such as
CO2, H2O, and energy.
Treatment technologies, which can be grouped as stirred tank reactor technologies
(CAS, oxidation ditch, A2O, and SBR), membrane technology (MBR), and biofilm technologies (MBBR, IFAS, DSFF, PBBR, FBBR, SFBBR, IFBBR, and SBBR) have evolved over
the years as governments around the world continue to raise the bar of quality standards of
wastewater-treated effluents. Advancements in treatment technology have put treatment
processes ahead of future challenges such as increased wastewater generation as a result
of the increasing global population, old and aging facilities, reduced installation spaces,
economic considerations, and climate change. Activated sludge technology (CAS) being the
oldest (developed around 1914) biological wastewater treatment technique, has undergone
several improvements for enhanced nutrient removal, increased surface area for microbial
growth, compact size, and cheaper capital costs, to technologies such as A2O, oxidation
ditch, and the SBR. Developments in treatment technologies shifted to better sludge
handling between the early 1970s and late 1980s, hence, the development of membrane
technologies, that is, the MBR technology, which offered maximum sludge separation from
treated water in the membrane media. However, membrane clogging due to biofouling in
MBR systems led to the development of MBBR systems around the mid-1990s, with lower
biofouling and clogging. The IFAS technology is the most recently developed biofilm technology, and it was deployed around the early 2000s. The technology was developed to mitigate the operational challenge of the slow biofilm growth rate of traditional MBBR systems,
is more energy efficient, and has a low capital cost compared to other biofilm technologies
including DSFF, PBBR, FBBR, and SBBR; although clogging is better managed in some of
these technologies (especially in the MBBR due to the movable biocarrier medium) than in
the IFAS system. New developments in IFAS systems are focused on sustainability with the
incorporation of mechanisms for methane production and capturing, and energy generation. Overall, biofilm wastewater treatment technology has a better volumetric capacity and
biomass retention period, higher biomass concentration, requires smaller installation space,
low hydraulic retention time, and sludge production when compared to stirred tank reactor
technology, although it has poor mass transfer, which affects the rate of reaction.
31
Wastewater Treatment – Past and Future Perspectives
Future trends in biological wastewater treatment technologies will focus on process
sustainability via energy generation to lower operational costs, compact systems, and
large-volume wastewater handling all of which can be provided by the biofilm reactor
technologies MBBR, IFA, MES, and even non-bacterial treatment systems like phytoremediation and algal-based treatments. Future designs and optimization of MBBR and
IFAS operations should focus on biocarrier configuration, geometry, and design material.
Author details
Olawale Theophilus Ogunwumi1*, Adeyemo Festus Adeniyi2, Mezie Chinazor Angus3
and Oche Sunday Oche4
1 Water Quality and Wastewater Treatment Research Laboratory, Chemical
and Petroleum Engineering Department, University of Lagos, Nigeria
2 Energy and Sustainability Research Laboratory, Chemical and Petroleum
Engineering Department, University of Lagos, Nigeria
3 Department of Corrosion Science and Engineering, Chukwuemeka Odumegwu
Ojukwu University (COOU), Anambra State
4 Department of Chemical and Petroleum Engineering, University of Lagos, Nigeria
*Address all correspondence to:
[email protected];
[email protected]
© 2024 The Author(s). Licensee IntechOpen. This chapter is distributed under the terms of
the Creative Commons Attribution License (http://creativecommons.org/licenses/by/3.0),
which permits unrestricted use, distribution, and reproduction in any medium, provided
the original work is properly cited.
32
Biological Wastewater Treatment
DOI: http://dx.doi.org/10.5772/intechopen.1004638
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