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Sanitary and environmental aspects of sewage sludge management

Currently, sewage sludge management is a huge challenge in the field of environmental engineering. New effective solutions for the treatment of wastewater led to an improvement of the quality of the final effluent but considerably increased the volume of produced sewage sludge, which increases each year. Two points of view conflict regarding the recycling of those “wastes.” Primarily, dehydrated sewage sludge is considered a reservoir of nutrients and organic matter that can be used as a fertilizer in agriculture or as an organic amendment in the remediation of contaminated sites or to build “anthroposoils.” On the other hand, recycled sewage sludge is seen as a potential source of soil contamination by organic and inorganic pollutants and pathogens; potentially toxic elements (such as zinc, copper, cadmium, lead, silver, etc.); polycyclic aromatic hydrocarbons (PAH); polychlorobiphenyls (PCB); biocides and phytopharmaceuticals; pharmaceuticals, personal care products (PPCP), and residuals; synthetic hormones; microplastics; nanotechnology life cycle end products; and microorganisms such as Escherichia coli O157:H7 or Salmonella typhimurium .

This chapter will focus on these aspects, highlighting the health and ecotoxicological risks associated with the presence of such contaminants in sludge. The environmental dangers of sludge spreading on soils will be presented as well as their possible treatment scenarios to propose an acceptable reuse of sewage sludge in a circular economy.

1. Introduction

Globally, 80% of wastewater is discharged untreated into the world's waterways ( Opec, 2018 ). Failure to treat effluents constitutes a serious threat to the environment, the climate, and human health, but this can also be considered a waste of resources. According to the goals of sustainable development and a circular economy, the wastewater shall be considered primarily as a source of water, then energy, organics, metals, and other resources. Consequently, sewage sludge is recognized as a source of renewable energy and material recovery ( Christodoulou and Stamatelatou, 2016 ). Thus, no longer considered a “waste,” it became a byproduct to be posttreated in order to be recycled into nature as energy, matter, or both. Sewage sludge is a reservoir of organic matter and nutrients, so it constitutes a potential substrate for a variety of possible reuse scenarios. Therefore, all potentially applied strategies shall fulfill the requirements of ecoinnovation. Thus, they shall lead to an important reduction of the negative environmental impacts by decreasing the consumption of natural resources or the release of harmful substances ( Rorat and Kacprzak, 2017 ). Consequently, contemporary trends in organic waste treatment follow the sustainable development strategy in terms of environmental, economic, and social impacts. The composition of sewage sludge is highly variable and may depend on many various factors such as the seasons, the technology applied in wastewater treatment plants (WWTPs), the specificity of the source area of the influent, etc. On average, dewatered sewage sludge contains 50%–70% organic matter and 30%–50% mineral components (including 1%–4% of inorganic carbon), 3.4%–4.0% nitrogen (N), 0.5%–2.5% phosphorus (P), and significant amounts of other nutrients, including micronutrients that could be recovered. For instance, extractable resources such as phosphorus (P) are predicted to become scarce or exhausted in the next 50–100 years, thus P recovery from wastewater is becoming an increasingly viable alternative ( Connor et al., 2017 ). Nevertheless, a relatively low content of lignin and cellulose makes the organic matter easy to decompose. Hence, it degrades fast and can cause a sharp peak in the nitrate and pollutant concentration in the soil if applied without pretreatment. The biggest challenge, though, is seen in the contaminants, (1) organic (such as polycyclic aromatic hydrocarbons (PAH), polychlorinated biphenyls (PCB), adsorbable organohalogens (AOX), pesticides, surfactants, hormones, pharmaceuticals) and (2) inorganic (metals and their nanoparticles), and (3) pathogenic species of living organisms for example, bacteria, viruses, protozoa, and parasitic helminths (see review by Fijalkowski et al., 2017 ).

In this context, this chapter focuses on the sanitary and environmental dangers of the presence of the above-mentioned contaminants in sludge. The environmental risks of sludge spreading on soils will be presented as well as their possible treatment scenarios to propose an acceptable reuse of sewage sludge in a circular economy.

2. The global production of sewage sludge and the main directions of its management

At the European scale, the 91/271/ECC urban wastewater treatment directive adopted in May 1991 imposed the collection and treatment of wastewater in agglomerations with a population equivalent (PE) of more than 2000. Consequently, the substantial and constant increase of wastewater sludge and its disposal are becoming a growing challenge for municipalities in Europe. The annual sludge production in EU-27 will grow from 11.5 million tons of dry solids (DS) in 2010 to 13 million tons DS in 2020 ( EC, 2008 ).

Table 1 shows the more recent data considering the production and disposal of sewage sludge for selected countries, according to OECD. While legislation more or less compels European countries to improve their sewage sludge management policies, many poor and developing countries are still studying possible wastewater treatment practices. For instance, the Federated States of Micronesia dumped almost 30% of produced sludge into the Pacific Ocean without any pretreatment in 2012 ( Rouse, 2013 ).

Sewage sludge production and disposal in selected countries in 2012

CountryProduced sewage sludgeTotal disposalAgricultural useCompost and other applicationsLandfillDumping at seaIncineration
Austria2662664074140139
Belgium15710719n.d.n.d.089
Czech Republic2632637215413n.d.8
Denmark14111574n.d.1034
Estonia161614n.d.20..
Finland14114179310032
France987932684n.d.400207
18491844542294001009
Greece11911914040039
Ireland7272684000
118350n.d.0693113928451110
Luxembourg854n.d.001
Netherlands3463250000321
Poland5335331153347057
Portugal339113102n.d.1100
Slovenia2626021013
Spain275725771922n.d.3840100
Sweden2071964867701
United Kingdom11371078844n.d.50229

n.d. , no data.

The global population exceeded 7.5 billion this year and is expected to surpass 9 billion by 2050. Urban populations may rise nearly twice as fast as they are projected to nearly double from 3.4 billion in 2012 to 6.4 billion by 2050, especially in developing countries, where the number of people living in slums may rise even faster, from 1 billion to 1.4 billion in just a decade ( Matiasi, 2012 ).

2.1. Sewage sludge as a substrate—Characteristics

The composition of sewage sludge is highly changeable during the process and also varies a lot between wastewater treatment facilities. Typically, raw (untreated) sewage sludge contains 2.0%–8.0% total dry solids (TS), 60%–80% of TS of volatile solids (VS), grease and fats, proteins, nitrogen, phosphorus, potassium, cellulose, iron, silica, alkalinity (mg/L as CaCO3), and organic acids (mg/L as Hac) ( Metcalf and Eddy, 1991 ).

The potential danger of using raw sewage sludge (not stabilized, only mechanically treated) for the sewage-to-matter final disposal strategies is huge due to the presence of pathogenic organisms and other contaminants. Therefore, some stabilization processes shall be applied at the WWTPs. The choice of applied technology depends strongly on the characteristics of raw sludge. Some parameters are crucial for the processes of stabilization, for example, pH, organic acid content, and alkalinity limit the anaerobic digestion process ( Metcalf et al., 2013 ) while pH, ammonia, and other parameters are important for the composting and vermicomposting processes ( Suleiman et al., 2017 ).

Fig. 1 presents the most typical pathways of sewage sludge treatment, including the processes at the WWTPs (thickening/stabilization/dewatering) and final disposal strategies. After thickening, sludge stabilization is usually performed. It is crucial for the further applications and aims primarily to reduce the potential risks by lowering the number of pathogens in organic matters. Two types of stabilization of liquid sewage sludge shall be distinguished:

  • 1) Chemical stabilization by the addition of lime to alter the value of the pH to > 11; eliminates the microbiological risk.
  • 2) Biological stabilization, meaning anaerobic or aerobic digestion. Aerobic digestion is a process of treating the secondary sludge from the biological wastewater treatment process as activated sludge or trickling filters; anaerobic digestion can be conducted in low (< 10%) as well as medium (15%–20%) and high 22%–40% solid anaerobic digestion systems; this technology is described in detail in the next section.

Fig. 1

Typical sewage sludge treatment process including processes at wastewater treatment plants (thickening/stabilization/dewatering) and the most common final disposal strategies applied worldwide.

After stabilization, the sludge shall be dewatered. Usually, this process is carried out using filter presses or centrifuges. As proper dewatering is crucial for the further disposal of sewage sludge, often an additional step of conditioning is required. The conditioners, synthetic organic polymers, or metal ions (typically iron salts) are used in order to coagulate the colloids in sludge and thus fasten the dewatering process ( Novak, 2006 ). Only an efficient stage of water removal allows applying efficiently the selected techniques of final treatment and disposal of sewage sludge.

2.2. Sewage sludge final treatment and disposal

The main directions for sustainable sewage sludge management are:

  • a) Matter recovery (sewage-to-matter): use in agriculture (directly as a fertilizer) and remediation of devastated or degraded lands.
  • b) Energy recovery (sewage-to-energy) by incineration and alternate thermal methods as pyrolysis, quasipyrolysis and gasification or coincineration (in cement plants). Wastewater contains a chemical energy that shall be converted to the usable form and thus fulfill a part of the worldwide need for renewable energy sources ( Puyol et al., 2016 ). Different technologies can be used to transfer the excess sewage sludge into energy. This strategy has lately been of great interest. Primarily, it allows using the potential of sewage sludge without the environmental risks often discussed for land applications that could introduce contaminants into the soil. Moreover, it responds to a global call for renewable energy sources.
  • c) Others, such as landfilling or dumping at sea, which are forbidden by most countries but still practiced in some parts of the world, mostly in developing countries.

2.2.1. Anaerobic digestion

At first recognized mainly as a process of the stabilization of sewage sludge with the main aim of pathogen bacteria removal, now anaerobic digestion (AD) is often considered as a technically mature and cost-effective process that converts sludge into biogas ( Cao and Pawłowski, 2012 ). The produced biogas can be used for the self-purposes of WWTPs that are characterized by a high demand for electricity, up to 0.78 kWh per m 3 of treated wastewater ( Cano et al., 2015 ). Ideally, the process of anaerobic digestion shall fulfill this high demand. In order to increase efficiency and thus biogas yields, it was proposed to introduce the other ingredients in the so-called codigestion. For instance, Grosser (2018) used grease trap sludge and an organic fraction of municipal waste as cosubstrates in the process, which enhanced the efficiency of sewage sludge anaerobic digestion. Similarly, other organic wastes have been tested with success, for example, food waste, cheese whey, and olive mill wastewater ( Maragkaki et al., 2018 ). Thus, codigestion of sewage sludge can be understood as a method of management of different organic wastes. Nevertheless, it cannot be fully seen as a final disposal of sludge, as it generates another byproduct, digested sludge (digestate), that still contains a high quantity of nutrients and contaminants and must be treated. It was proven that the utilization of digestates may replace or reduce the use of mineral fertilizer in agronomic plant production, as it is rich in plant-available nutrients (ammonium, phosphate, and potassium) ( Sogn et al., 2018 ). Yet, in-land use as a biofertilizer is possible only if the product can be qualified according to applicable norms, usually regulated by soil protection legislation, fertilizer, or waste legislation. Otherwise, other options shall be considered. Lately, Peng et al. (2018) proposed using the digestate in landfill bioreactors in order to remove the nitrogen of old landfill leachate. Digestate was also successfully applied with other organic wastes as the organic fraction of municipal wastes, sawdust, and green wastes in the process of vermicomposting ( Rorat et al., 2017 ). As the chemical composition of digestate corresponds to the composition of the used substrates, the long-term effects of its introduction to the soil shall be studied in order to appreciate the impact on soil functions (soil biodiversity and microbial cycles). The existing studies focus mainly on the fertilizer properties of the digestates produced from different substrates. According to Nkoa (2014) , the most common risks associated with the application of digestate in land are related to:

  • a) Risks of atmospheric pollution (ammonia emission and fallout, nitrous oxide emission).
  • b) Risks of nutrient pollution (excess nitrogen and phosphorus).
  • c) Risk of soil contamination (chemical/biological contamination).

2.2.2. Composting and vermicomposting

Composting as a method of biological decomposition of biowastes in the presence of oxygen contributes powerfully to the recycling and conservation of several macro- and micronutrients from sewage sludge in the soil. Its alternative, vermicomposting, is a modern, inexpensive, and eco-friendly biotechnology in which earthworms are employed as natural bioreactors in order to decompose the organic matter ( Suleiman et al., 2017 ). Their metabolic activity and cooperation with microorganisms lead to a 40%–60% reduction of volume, an increase of bioavailability of nutrients to plants, a reduction in the C/N ratio, and a decrease of the availability of some dangerous contaminants such as metals ( Rorat et al., 2015 ). Although composting can be considered highly beneficial and a low cost sewage-to-matter strategy that allows recycling organic nutrients into the ecosystem, it still causes some important problems from an environmental point of view. Due to the rapid degradation of nitrogenous organic matter, important nitrogen losses and greenhouse gas (GHG) emissions can be noted ( Sánchez-Monedero et al., 2010 ). Those effects can be partially reduced by the introduction of different bulking agents, for example, agricultural wastes and alkaline amendments such as lime, zeolite, and bentonite. Recently, biochar has also been considered an efficient agent causing a reduction of greenhouse gases, ammonia, and extractable ammonia emissions ( Malińska et al., 2014 ; Awasthi et al., 2016 ). Although these effects can be partially eliminated, researchers are concerned about the input of potentially toxic metal elements and therefore their possible accumulation for several in the soil horizon ( Fang et al., 2017 ). The same type of risk is related to the presence of other chemical compounds and pharmaceuticals as well as some pathogens that can survive the process.

2.2.3. Thermal processes

All thermal processes are considered sludge-to-energy systems that lead to the complete oxidation of the volatile matter with production of a residue (ash). Generally, the most famous technologies are incineration, gasification, pyrolysis, and plasma gasification. Combustion and/or incineration are considered the most attractive disposal methods for sewage sludge in Europe ( EC, 2008 ), as they replace potentially dangerous landfilling and agricultural strategies. This also allows largely reducing the volume of sewage sludge to destroy the microbiological danger, minimize the odors, and simultaneously recover the renewable energy. Three main variants of this process are used: incineration in dedicated plants, coincineration with municipal solid wastes, and incineration in cement kilns. The environmental cost related to those systems is mostly related to the high energy consumption and production of harmful gaseous emissions (i.e., dioxins and furans) ( Garrido-Baserba et al., 2015 ). Moreover, the ashes coming from the process can be considered a concentrated pollutant that accumulates chemical contaminants. The interesting alternative for ash disposal is a cement replacement. After incineration, sewage sludge is still rich in silica, alumina, calcium oxide, and iron oxide, so it can be used in the production of building materials. Moreover, in this form, metals are stabilized and solidified, so the potential risk is reduced ( Samolada and Zabaniotou, 2014 ).

Pyrolysis is being recognized as a relatively expensive but highly effective technology. Basically, the process converts the organic matter into bioenergy (oil/gas) with a byproduct in the form of so-called biochar. Thus, pyrolysis allows yielding a major bio-oil fraction potentially useful as a fuel or as a source of chemical products. Generally, pyrolysis and similar processes of combustion of sewage sludge are regarded as endothermic. Nevertheless, Atienza-Martínez et al. (2018) have shown lately that the necessity of pretreatment of this substrate (dehydration) moves it more to the exothermic processes, although it is still the most cost-consuming throughout the scenario. Thus, improvement of the steps allowing water removal is crucial for the future potential of the process. Independently, numerous studies have shown many advantages of using biochar for environmental management. For instance, it can be applied for soil improvement, to improve the efficiency of the resources, for remediation and/or protection of lands, and future greenhouse gas mitigation ( Joseph and Lehmann, 2015 ). In general, biochar can thus be defined as a solid, carbon-rich material obtained in the process of zero or low oxygen pyrolysis from different C-based feedstocks, which, applied to the soils, sustainably sequesters carbon and thus improves soil quality in the long term ( Verheijen et al., 2010 ).

As far as the process of combustion eliminates the microbiological risk related to the land application of sewage sludge, still some questions considering chemical pollutants are being posed. These need to be evaluated on a case-by-case basis, not only with concern to the biochar product itself but also to soil type and environmental conditions ( Verheijen et al., 2010 ). Nevertheless, lately it has been recognized that the addition of activated carbon or biochar to sewage sludge immobilizes the bioavailable fractions of polycyclic aromatic hydrocarbons and metal elements ( Kończak and Oleszczuk, 2018 ). Moreover, Frišták and Soja (2015) recognized that the addition of biochar produced from wood chips and garden residues into the sewage sludge and its application as soil amendments have increased the content of available forms of phosphorus. The positive effects of the addition of sewage sludge-derived biochar were also observed during the process of vermicomposting of sewage sludge, where it significantly reduced the bioavailability of Cd and Zn for Eisenia fetida earthworms ( Malińska et al., 2017 ).

3. Sewage sludge as sources and drive pathways for contaminants

Considering all valuable resources present in sewage sludge (organic matter, plant culture available nutrients), many countries recognized this byproduct as a potential substrate for fertilization in agriculture or remediation of polluted areas. Nevertheless, sewage sludge applications on agricultural land might contribute to the dispersal of a broad range of unwanted constituents on soils possibly used for food production. Such undesirable contaminants (potentially toxic elements (PTE) such as metals, trace organic compounds (TrOC), and pathogenic organisms) may pose sanitary and environmental risks ( Andreoli et al., 2017 ). Toxic pollutants in sewage sludge could even, in some cases, increase preexisting environmental problems and lead to secondary environmental contaminants and poisonings if not properly managed.

As a reflection of our chemical-based consumer society, our wastewater and sewage sludge mirror compounds we use, produce, release, and discharge. Sludge composition, its agronomic interests, and contaminations may so differ greatly. Such parameters depend on the wastewater origins (agricultural, industrial areas or urban), the local household and consumer habits, the sewer collection (separation or not for wastewater and runoff), the regional environmental regulations, the season and obviously of the size and the process used by the considered WWTP.

3.1. Chemical contaminants in sludge

The environmental risk of sludge contaminants and their concentrations in soil after land application is dependent on their initial concentrations (in both soils and sludge) and the application rate (cumulative effects), management practices, and losses. Therefore, volatile and easily degradable contaminants may still pose environmental risks in the case of high initial concentrations and repeated applications ( Harrison et al., 2006 ).

There are two environmental and public health issues involved with the use or disposal of WWTP biosolids: potentially toxic elements (PTEs) and organic contaminants (OCs), chiefly persistent chemicals. Concerns relate to potential trophic transfers (via cultivated plants) and possible contamination of groundwater. PTE is a common general term that includes metal elements, formerly known as “heavy metals” or “metal trace elements.” They are naturally present in soils and the current concerns come more from anthropogenic soil contamination by these elements through the use of fertilizers (including sludge, slurries, and manures), pesticides, and poor waste management. They classically comprise the following metals and metalloids: arsenic (As), cadmium (Cd), chromium (Cr), copper (Cu), lead (Pb), mercury (Hg), molybdenum (Mo), nickel (Ni), and zinc (Zn). Potential environmental risks associated with these PTEs in the context of sludge land applications have been extensively studied and environmental guidelines and regulations defined. For several OCs, such a regulatory framework exists as for polycyclic aromatic hydrocarbons and several persistent organic pollutants (POPs, such as PCBs, dioxins, and related compounds (PCDD/F)). The list and limit values for concentrations of metal elements and OCs that should restrict the use of sewage sludge in agriculture have been updated recently in Europe ( EC, 2000 ). They have suggested the regulation of linear alkylbenzene sulfonates (LAS; extensively used as surfactants), Di(2-ethylhexyl) phthalate (DEHP), nonylphenol and nonylphenol ethoxylates (NP(E)), halogenated organic compounds (i.e., adsorbable organic halides (AOX)), PAH, PCBs, and polychlorinated dibenzo-p-dioxins and dibenzo-furans (PCDD/F). Studies on sludge contaminants started in the 1970s. Most of the chemicals we use in our everyday lives and those with industrial applications are likely to end their lifecycle in biosolids, not to mention byproducts of human activities. We could only exclude highly volatile products and those that are rapidly degraded. In addition to the OCs in urban wastewaters, surface run-off of atmospheric-deposited environmental contaminants onto artificialized areas (concreted and paved, consequently impervious) contribute to the accumulation in sewage sludge of lipophilic compounds that tend to adsorb to solid particles. This situation is like that of sediments in aquatic ecosystems. It is the nonpolar and some persistent compounds that could represent an environmental risk with sludge recycling. One of the most concrete examples may be that of surfactants such as LAS (little worrying, even considering present uses but above all realized risk assessments, ( Schowanek et al., 2007 )) and more worrisome fluorosurfactants such as perfluorooctanesulfonic acid (PFOS), perfluorooctanoic acid (PFOA), and perfluorononanoic acid (PFNA) ( Smith, 2009 ).

As an introduction to their review of emerging OC in sludge, Clarke and Smith (2011) considered that of the 100,000 chemicals registered in the EU, all are likely to be found in WWTP sludge. In 1996, Wilson et al. (1996) proposed a list of 300 products to prioritize in sludge research work and surveys (priority organic pollutants on environmental agency and country lists and compounds identified in sludge worldwide). This number is close to the one (332) from ( Drescher-Kaden et al., 1992 ) on toxic or suspected toxic OC residues in German sludge, based on a review of the literature on more than 900 articles. Harrison et al. (2006) reported 516 OCs for which concentration data were available in the peer-reviewed literature and official government reports. More recently, Eriksson et al. (2008) concluded after a literature review that 541 OCs could potentially be present in sewage sludge due to their use in construction materials, pharmaceuticals, and personal care products. However, some OC concentrations are not sufficiently characterized in such matrices as sludge and biosolids because their analyses are confined on regulated or identified contaminants on priority lists that represent only a small fraction of the present OCs ( Harrison et al., 2006 ). These authors highlight the lack of knowledge for OCs as nitrosamines with high environmental risks while the knowledge is more comprehensive for some families such as pesticides, PAHs, and PCBs. Thus, a global vision of the contaminants present in the sludge is possible for some as metals, PCB, PAH ... Besides, the concentrations for these compounds in sludge tend to decrease. As an illustration of sludge contaminations around the world, we propose Table 2 , Table 3 . Such an overall worldwide inventory could also be made for PCBs and PCDD/Fs, but it would not be possible for most other TrOCs.

Total concentrations (averages of selected metals present in sewage sludge of different countries worldwide)

Total element concentrations (mg/kg of dry sludge solids; except specific units for several values) Comments and references
AgAlAsCdCrCuFeHgNiPbZn
Braziln.r.n.r.14.6910.75143.72255.39n.r.2.3541.9980.37688.83Averaged values in wastewater sludge ( )
Canadan.r.n.r.n.r.2.3–1066–2021180–2300n.r.n.r.37–17926–465354–640( ; ; ) In ( )
n.r.n.r.1150460n.r.11651593Averaged values in Biosolids, Ottawa; British Columbia and Greater Moncton Sewerage Commission ( )
n.r.n.r.4.62.350.7888n.r.3.126.456588
n.r.n.rn.r.0.5n.r.137n.r.0.3927223
Chinan.r.n.r.16.7–265.9–1345.8–78.4131.2–394.5n.r.17–2449.3–95.557.5–109.3783.4–3096Min and max six plants ( )
n.r.n.r.n.r.2.1–19.422.2–453.2210.6–1191.3n.r.n.r.25.1–106.641.2–452.21406.2–3699.2Min and max 12 plants in Zhejiang Province ( )
n.r.n.r.n.r.1.651983.83323.9n.rn.r.422.069.72424.2Xiamen WWTP, Fujian Province ( )
n.r.n.r.n.r.11.72, 9.63–15.13112.5, 50–125383.47, 62.75–796.63n.r..n.r.692.94, 98.63–2180.13113.19, 86.25–136.75609.44, 290.38–831Mean, min and max four plants ( )
n.rn.r.n.r2.12514.24266.06n.rn.r84.64n.r.1345.51Raw sludge from the Shihezi WWTP, Xinjiang ( )
Colombian.r.n.r.18.67672.5163.4n.r.842.987.51014.2Averaged values in biosolids from El Salitre WWTP, Bogota ( )
Finlandn.r.n.r.n.r.0.618.1244n.r.0.3730.38.8332Averaged values in 2005 wastewater sludge ( )
Francen.r.n.r.n.r.4.564286n.r.2.135107761Median of 237 mainly domestic WWTP, ( )
Germanyn.r.n.r.n.r.1.550275n.r.n.r.23.367.7834( ). In ( )
n.r.n.r.n.r.1.5260.5380.2n.r.0.9232.261.7955.7Averaged values in 2003 wastewater sludge—DWA survey ( )
Hong-Kongn.r.n.r.n.r.n.r.663112–255n.r.n.r.44.5–62252.5–571009–2823( ; ) In ( )
Indian.r.n.r.n.r.41–54102–8810280–543n.r.n.r.192–29391–129870–1510( ; ) In ( )
Irann.r.60–259n.r.6.1–15.32782–807157.5–163n.r.n.r.17.9–59.3n.r.260–2077Mean, min and max four plants ( )
Irelandn.r.n.r.n.d.1235520n.r.n.d.18252886Averaged values from 16 plants ( )
Italyn.r.n.r.7.32.762.1601n.r.n.r.29.216.3961Sludge from the municipal WWTP of Brindisi ( )
n.r.n.r.n.r2.1n.r.370n.r.n.r.19721500( ) In ( )
n.r.n.r.n.r0.3–0.918–6590–206n.r.0.2–0.911–1580–126283–895Range three plants ( )
n.r.n.r.n.r1.622.3261n.r.0.215.676.2577Averaged values in 2006 Sardinia biosolids used in agriculture ( )
Japann.r.n.r.8.22.219.5n.r.n.r.1.132.35.2n.r.Averaged values in dried wastewater sludge, Suzu ( )
Polandn.r.n.r.n.r.n.d.58194n.r.1.042223.51459Mean values in sludge from the treatment plant of Sokółka ( )
n.r.n.r.n.r.1.6316.1191.4n.r.0.45715.632.41248.5Sludge from a small, a medium and a large WWTP in Central Poland ( )
n.r.n.r.n.r.n.d.17.2158.0n.r.0.29717.650.4962.9
n.r.n.r.n.r.1.3637.255.8n.r.0.234n.d.n.d.344.8
Netherlandsn.r.n.r. ; ; – ; – n.r. ; ; – ; – ; – Range values from Dutch and WWTP sludge ( )
Russian.r.n.r.n.r.n.r.305–310200–300n.r.11.3575–7734.70.07–0.08 (%)( ) In ( )
n.r.n.r.0–240–30018.2–12800.9–1200n.r.0–11.351.4–3060.8–10703.0–3820Range values in 2017 sludge from Moscow Area ( )
Slovenian.r.n.r.2190200n.r.235150600Averaged values in wastewater sludge ( )
Spainn.r.n.r.n.r.2.37–18.354.4–3809204–337n.r.n.r.23.2–36.5167–223871–1626( ) In ( )
Sweden1.98n.r.n.r.2.10n.r.323n.r.1.4517.345720Mean, min and max 11 plants ( )
0.72–3.260.59–37110–6400.19–107.3–3610.9–560396–1500
South African.r.n.r.n.r.0.82–3.1035.07–134.08263.68–626.00n.r.n.r.31.34–51.4321.28–171.871031.75–1732.00Min and max 5 plants, Limpopo province ( )
Turkeyn.r.n.r.n.r.1.2434.270.2n.r.n.r.62.134.2300Averaged values in Izmir et al., 2008) Guneybati WWTP sludge ( )
0.1–14.70.1–60 (%)5.1–56.10.3–5.110.8–1542.227.3–578.10.2–14.9 (%)0.1–1.18.6–3104.0–429.80–0.1 (%)Range values adapted from ( ) In ( )
n.r.n.r.n.r.0.4–3.816–27539–641n.r.0.3–39–9013–221142–2000Typical ranges from ( ) In ( )
UKn.r.n.r.n.r.3.5159.5562n.r.n.r.58.5221.5778( ; ) In ( )
USAn.r.n.r.n.r.25178616n.r.n.r.711701285( ) In ( )
n.rn.r.2.62n.r670n.r.1.31639743Averaged values in class B biosolids—Denver and Los Angeles Hyperion Treatment Plant ( )
n.rn.r.6.0610.2841060n.r.1.9150.838.51180

WWTP , wastewater treatment plant; n.r. , not reported; n.d. , not detected or under quantification limits.

Total concentrations (average or range values) of selected PAH congeners in sewage sludge of different countries worldwide

Concentrations of individual PAH ( g/kg of dry sludge solids except specific units for several values) Comments and references
NaAceAcFlPhenAntFluoPyrB[a]AChB[b]FB[k]FB[a]PD[ah]AB[ghi]PInd∑ PAH⁎
( g/kg dry matter)
China16.23–180.9520.08–289.863.11–131.1417.37–91.7748.37–466.4122.46–214.44138.40–658.33120.47–317.31170.58–2171.24493.89–2958.66572.71– 115.07–2138.07226.73–6174.17 –1134.62 1038.67 2682.702467.32–259723.79Min and max six plants, Beijing ⁎(16 US EPA) ( )
140–1632020–6570 3890490–11940 40–6140620–9880 15680180–4820470–11200 10800–2170230–7850 –14050 –6520 –937033730–87500
13890–641200
Min and max 12 plants ⁎(16 US EPA and 9 EC) ( )
Czech Republicn.r.n.r.n.r.n.r.17–3910n.r.12–877.99.5–2869.9n.r.n.r. 21.5–2468.4n.r.312.1–2724.6305.3–2905.41481.3–17313.6Min and max values of 45 samples of sludge ( ) In ( )
Francen.r.n.r.n.r. n.r.n.r.40n.r.n.r.n.r.30n.r. n.r.n.r.n.r.n.r.Min, max and mean in sludge collected along the treatment process of Seine Aval treatment plant ( )
630
240370
Italyn.r.000000000000000n.r.Sludge from the municipal WWTP of Brindisi ( )
n.r.n.r. 1–2281–673n.r.2–8441–1118n.r.n.r.2– 1–1341n.r.1–10301–131011–3917Min and max values from 35 WWTP in northern Italy 452 samples—survey of four years ⁎(9 EC) ( )
Jordan1.9n.r. 0.53.00.4 4.22.01.92.11.01.90.44.71.434.6WWTP sludge from an University complex or a municipal area and sludge from a raw wastewater and sludge disposal site, Karak ⁎(∑ 16 with B[e]P instead of Ace) ( )
3.00.31.94.83.93.36.2 1.80.90.41.2 1.239.3
1.10.43.5 0.51.44.80.71.2 0.30.5 6.3 28.7
Japann.r.3.32.53.912.62.614.7 3.63.64.434.31.62.8 82Mix of six dewatered WWTP sludge: rural, urban and residential areas ⁎(∑ 16 with B[e]P instead of Na) ( )
Malaysia n.r.n.r.n.r. 4070n.r. n.r.n.r.n.r.n.r.n.r. n.r.n.r.n.r.n.r.Min and max from three plants, Johore ( )
Poland 68.717.9 84.8 214.5 134.7 88.22039.9Min, max and mean of 15 municipal sewage treatment plants ⁎(16 US EPA) ( )
2946.5974.21149.2425.55399.95050.52579.31869.17572.5 1786.0458.9835.11395.636034.1
886.6199.6526.7165.91937.81096.3918.5577.31857.3 610.772.3262.6368.811612.9
0.00790.08850.0960.12990.2822 0.61150.12950.15430.07150.05240.04230.08220.01760.1295n.r.Mean values in sludge from the treatment plant of Sokółka ( )
2.0332.125.47.814.8817.111.30.470.850.120.130.12 0.0220.028183.1Freely dissolved PAHs in municipal WWTP sludge, Chełm ⁎(16 US EPA) ( )
(ng/L)(ng/L)(ng/L)(ng/L)(ng/L)(ng/L)(ng/L)(ng/L)(ng/L)(ng/L)(ng/L)(ng/L) (ng/L)(ng/L)(ng/L)
Portugal27–198 –118 –49228–704540– 34–234100–629277–70280–18479–31235–47911–28923–522 –66 –589 –4612510–5520Range values from two domestic and four industrial WWTP sludge ⁎(16 US EPA) ( )
–309 –30 –7277–909250– –29256–685112–70629–15513–283 –234 –9517–275 –1250–16027–2951130–4120
Romania n.r.0.0040.0220.0700.005n.r.0.0240.009 0.0050.0010.0030.0090.0320.022n.r.Averaged values in primary and in digested dehydrated sludge of Cluj-Napoca WWTP ( )
0.0070.0260.0600.0040.0000.004 0.002 0.0010.0030.0230
Spainn.r.n.r. –300 –75020– n.r.33–570 –731n.r.n.r. –242§ –242§17–100n.r. –88308–5118Min and max values of 38 samples of sludge ⁎(9 EC) ( ) In ( )
Turkeyn.r.n.r.n.r.n.r. –1164.5n.r.12– 9.5–2869.9n.r.n.r.434.4– 21.5–2468.4n.r.312.1–2724.6305.3–2905.41481.3–17313.6Min and max values of 14 samples of sludge ⁎(9 EC) ( ) In ( )
UE countriesn.r.n.r.n.r.n.r.29.9–552.215.3–724.034.5– 47.2–2637.0 –1832.621.0–2020.525.1–1919.49.9–1048.017.9–1475.5n.r.n.r.n.r. Range values and occurrence adapted from ( ) In ( )
100%84%100%100%97%94%91%100%100%
n.r.n.r.n.r.n.r.29.9–552n.r.34.5–321747.2–2637n.r.n.r.17.9–1476 29.7–133524.2–1401 Min and max values of 32 samples of sludge from member states ( ) In ( )
UKn.r.n.r.1700–6600 –81003200– n.r.1400–74002100–5600n.r.n.r.1800–11700§1800–11700§690–4000n.r.470– –270018000–50000Min and max values of 14 samples of sludge ⁎(9 EC) ( ) In ( )

Less and more present congener reported values in a table line are in bold. Abbreviations: n.r. , not reported; 0 , not detected or under detection or quantification limits. Na , Naphthalene; Ace , Acenaphthylene; Ac , Acenaphtene; Fl , Fluorene; Phen , Phenanthrene; Ant , Anthracene; Fluo , Fluoranthene; Pyr , Pyrene; B[a]A , Benz[a]anthracene; Ch , Chrysene; B[b]F , Benzo[b]fluoranthene; B[k]F , Benzo[k] fluoranthene; B[a]P , Benzo[a]pyrene; B[e]P , Benzo[e]pyrene; D[ah]A , Dibenz[a,h] anthracene; B[ghi]P , Benzo[ghi]perylene; Ind , Indeno[1,2,3-cd]pyrene.

16 US EPA priority PAH: acenaphtene, acenaphthylene, anthracene, benzo[a]anthracene, benzo[b]fluoranthene, benzo[k]fluoranthene, benzo[ghi]perylene, benzo[a]pyrene, chrysene, dibenzo[a,h]anthracene, fluoranthene, fluorene, indeno[1,2,3-cd]pyrene, naphthalene, phenanthrene and pyrene.

9 CEC: EU proposed sum of PAHs (acenaphthene, fluorene, phenanthrene, fluoranthene, pyrene, benzo[b + j + k]fluoranthene, benzo[a]pyrene, indeno[1,2,3-cd]pyrene, benzo[ghi]perylene) should not exceed 6 mg/kg dry matter. in sludge for land application) ( EC, 2000 ) ; § reported concentrations for benzo[b + j + k]fluoranthene; §§ reported concentrations for benzo[b + k]fluoranthene.

The first lesson of Table 2 on metal concentrations in sludge is that there is a real scientific consensus for these elements. Zn is always the predominant metal in terms of concentrations. PTE is one of the few families of contaminants for which sequential or selective extraction approaches could be used to approach the key issue in contaminant risk assessment, which is bioavailability. The origins of PTEs in wastewater are also well described and understood and even some technical solutions for metal removal from sludge have been developed and proposed (see ( Babel and Del Mundo Dacera, 2006 ) for an example of review).

The fact that PAHs ( Table 3 ) are priority environmental pollutants relies mainly on their possible harmful effects on biota as well as carcinogenicity in humans. They are too lipophilic with low biodegradability and they accumulate in sludge, sediments, and soils. The main sources of sludge PAH are industrial wastes as well as domestic sewage, atmospheric rainfall, precipitation of airborne pollutants, and road surface and tire abrasion products (PAHs) ( Bomboi and Hernandez, 1991 ). We will emphasize the study of ( Stefaniuk et al., 2018 ), which proposes to analyze the freely dissolved PAH concentrations rather than the total concentrations in order to better estimate their potential environmental availabilities.

For so-called “emerging” contaminants, scientific works appear and a global scheme is emerging since a decade. These contaminants are considered emerging because either the current analytical techniques finally allow their analyses in sludge, or the new industrial and domestic uses of certain products increase their concentrations in environmental matrices. Among these compounds are prominent pharmaceuticals, personal care products and residues, endocrine disruptors, and, more recently, nanoparticles and microplastics. In the excellent review of Clarke and Smith (2011) , these authors ranked the following biosolid emerging contaminants (priority decreasing order): PFOS and PFOA, polychlorinated alkanes, polychlorinated naphthalenes, organotins, polybrominated diphenyl ethers, triclosan, triclocarban, benzothiazoles, antibiotics and pharmaceuticals, synthetic musks, bisphenol A, quaternary ammonium compounds, steroids, phthalate acid esters, and polydimethylsiloxanes.

The field of such OCs in sludge as well as their fates and behaviors following sludge land application are largely to be investigated to finally allow their comprehensive risk assessment and case-by-case sludge environmental (even ecotoxicological) assessments must be favored.

3.2. Pathogenic organisms

Sewage sludge contains biological agents that can be problematic for living organisms because some are pathogenic or may simply disturb natural ecosystems. Generally, four groups of pathogens can be found in sewage sludge: viruses, bacteria, parasites, and fungi. In fact, due to its very rich organic matter, sewage sludge can include many bacteria and fungi species in large quantities ( Fijalkowski et al., 2017 ). Other organisms such as viruses and parasites are also regularly present in sewage sludge ( Frąc et al., 2014 ). The concentration and type of pathogen depend on the type of WWTP, the source of wastewater, and some environmental factors ( Romdhana et al., 2009 ). However, the majority of these pathogenic organisms are derived from human or animal feces ( Bloem et al., 2017 ).

The microbial flora present in sewage sludge is very diverse and abundant due to the high content of organic matter. The majority of these bacteria are saprophytes; they are safe and play an important role in the process of wastewater treatment by forming flocs and degrading some contaminants ( Tozzoli et al., 2017 ). However, some of these bacteria are pathogenic. Huang et al. (2018) identified 243 potentially pathogenic bacterial species in activated sludge, including six major pathogens ( Bacillus anthracis , Clostridium perfringens , Enterococcus faecalis , Escherichia coli , Pseudomonas aeruginosa , and Vibrio cholera ) that can reach abundances of 14% of the bacterial flora. Others pathogens such as Salmonella , Shigella , Klebsiella , Serratia , Enterobacter, or Proteus have also been identified ( Korzeniewska, 2011 ). All these bacteria may cause various infections such as urinary tract infections ( E. coli ), pneumonia ( Klebsiella and Enterobacter ), blood infections ( Enterobacteriaceae ), and gastrointestinal infections ( E. coli , Salmonella ). These diseases can appear after contamination by gastrointestinal, respiratory, urinary, and biliary tracts ( Korzeniewska, 2011 ).

E. coli is already part of one of the quality criteria for sludge (European Directive 86/278/EEC) ( EC, 1986 ). Also, Salmonella is one of the most-studied bacteria in WWTP sludge ( Jr Krzyzanowski et al., 2016 ). These bacteria can survive once released into the environment in part through sludge spreading on agricultural plots ( Jr Krzyzanowski et al., 2016 ; Bloem et al., 2017 ; Ellis et al., 2018 ). Thus, the consumption of food from these lands could be a way of contamination. It has been shown that even with low concentrations of Salmonella in sludge, some vegetables such as lettuce ( Manios et al., 2013 ) and tomatoes ( Asplund and Nurmi, 1991 ) may contain those bacteria in their tissues ( Jr Krzyzanowski et al., 2016 ).

The risk of the presence of pathogenic bacteria could be aggravated by the presence of antibiotics in wastewater. This increases the number of antibiotic-resistant bacteria. Moreover, the high density of bacteria in WWTP reactors increases the probability of transfer of genetic material between bacteria ( Turolla et al., 2018 ). In Austria, for example, Galler et al. (2018) isolated three multiresistant enterobacteria (extended-spectrum β-lactamase bacteria (ESBL)) from activated sludge: Gram-negative bacilli, methicillin-resistant Staphylococcus aureus (MRSA), and Vancomycin-resistant enterococci (VRE)). This could pose sanitary problems because of the dispersion of such antibiotic-resistant bacteria through trophic webs and in the environment ( Reinthaler et al., 2013 ; Fijalkowski et al., 2017 ; Tozzoli et al., 2017 ).

The microflora of sewage sludge is also very rich in fungi ( Frąc et al., 2014 ). Fungi play a crucial role in the treatment of wastewater by participating in the degradation of various contaminants ( Tozzoli et al., 2017 ). Several are nevertheless pathogens for plants. For example, two common phytopathogens, M. circinelloides and G. citri-aurantii , are regularly observed and they affect crop yield by causing diseases in fruits and vegetables. In addition to this ecological and environmental/agronomic risk, with fungi being opportunistic organisms, they have potential pathogenic properties for humans and animals as well ( Frąc et al., 2014 ). Frąc et al. (2017) have found in sewage sludge the fungus Trichophyton sp., which is responsible for dermatophytose.

Due to the origin of wastewater, sludge regularly contains viruses, especially of an intestinal origin. Schlindwein et al. (2010) highlighted the most common viruses in WWTP sludge samples from Brazil and tested their viability. The most common viruses were the adenovirus (AdV), the rotavirus (RV), the poliovirus (PV), and finally the hepatitis A virus (HAV). The viability of RV and HAV is around 15%–25% while that of AdV and PV is very high (100% and 90%, respectively), which shows that water and sludge treatment processes are not sufficient to inactivate viruses. This highlights the potential sanitary risks of the dispersal of sludge in the environment.

Furthermore, Bibby and Peccia (2013) found that the most abundant pathogenic viruses were herpes viruses in some US sludge samples. DNA viruses (adenovirus, herpes virus, papillomavirus, and bocavirus) are present in 90% of the samples, and RNA viruses (coronavirus, klassevirus, and rotavirus) are present in 80% of the sludge samples. These viruses can cause serious respiratory and gastrointestinal infections in humans and animals.

Like bacteria, viruses are able to survive once in the environment. Bloem et al. (2017) reported the persistence of enteric viruses for about 100 days in soils.

Works on sewage sludge also reported the presence of parasites such as nematodes and cestodes. Some of them are pathogens for humans and animals and are responsible for various diseases ( Chaoua et al., 2017 ). Sludge frequently contains helminth eggs ( Ascaris , Trichuris , Toxocara ) ( Da Rocha et al., 2016 ), which are among the most resistant organisms to sludge treatment. Their survival has already been observed for several years after the biosolid to soil application ( Bloem et al., 2017 ).

Other parasites of the protozoan family are also present. Corrêa Medeiros and Antonio Daniel (2018) observed the presence of protozoan cysts in 100% of the samples they controlled and the presence of oocysts in more than half the same samples. A change in sludge treatment had no impact on the concentration and viability of these protozoan forms. Families with some pathogenic species for animals and humans have been observed such as Cryptosporidium , Giardia, and Entamoeba ( Sabbahi et al., 2018 ; Khouja et al., 2010 ).

4. Conclusions and perspectives

Legislative pressure forces all countries to respect the common waste management hierarchy with prevention, reuse, recycling, and recovery the most preferable pathways while landfilling and disposal should be strictly limited ( Rorat and Kacprzak, 2017 ). Authorities, communities, wastewater industries should therefore apply environmental assessments as decision-making tools, in addition to the economic and technical evaluation of each proposed solution. Life Cycle Assessment (LCA) is a tool that allows quantifying the environmental impact/cost of particular options for management of sewage sludge in order to choose the best suitable option for each stakeholder. The result of an LCA shall be understood to be an environmental profile of total and single lifecycle stages considering the use of resources, human health, and ecologic consequences; it does not show any economic or social factors ( Cherubini et al., 2009 ). For instance, the impacts related to wastewater treatment could concern mainly: (1) energy consumption at different stages (global warming), (2) the presence of PTEs (toxicity) and (3) the content of chemical oxygen demand (COD), N and P (eutrophication) ( Feijoo et al., 2018 ). In the case of sewage sludge, most studies examine environmental aspects related to sludge application through fuel requirements (transport on agricultural land), introduction of metals into soils, the reduced use of mineral fertilizers, greenhouse gas emissions, carbon storage, and nutrient leaching ( Yoshida et al., 2013 ). Generally, land application is a contributor to global warming, eutrophication, and acidification while toxicity was considered to be related to the presence of Zn and Cu, according to ( Yoshida et al., 2018 ). Lundin et al. (2004) have compared four different options for final disposal of sewage sludge: agricultural application, coincineration with waste, incineration combined with phosphorus recovery, and fractionation with phosphorus recovery. In most aspects, the agricultural land disposal was recognized as the least preferable from an environmental point of view while other options have good potential of sustainability. Lately, Turunen et al. (2018) have developed a multiattribute value theory (MAVT)-based decision support tool (DST) in order to supply the simple scoring method to count the environmental risks of particular scenarios. The constructed value tree helped to select pyrolysis above the other tested alternatives of composting and incineration.

It is worth noticing that no universal solution can be pointed to as the environmental cost depends on local conditions, which can be highly variable between regions/countries. Often, the decision-making tools omit the problems of the properties of soil, climate, fauna, and flora present in the environment that can also greatly change the final impact of the sewage sludge on the ecosystems. Unfortunately, the most important decisions considering the treatment of sewage sludge are still being made based on economic and political criteria.

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Sewage Sludge Management for Environmental Sustainability: An Introduction

  • First Online: 01 January 2022

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literature review on sewage sludge

  • Jussara Borges Regitano 6   na1 ,
  • Mayra Maniero Rodrigues 6   na1 ,
  • Guilherme Lucio Martins 6   na1 ,
  • Júlio Flávio Osti 6   na1 ,
  • Douglas Gomes Viana 6   na1 &
  • Adijailton José de Souza 6   na1  

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1 Citations

The environmentally sound management of the increasing amounts of sewage sludges generated in urban centers is one of the greatest challenges of modern society. It is estimated more than half of the world’s population will be concentrated in urban areas by 2050. Sewage sludges contain organic matter and nutrients that can be reused in agriculture, but the public is concerned about its potential to contaminate natural ecosystems spreading hazardous trace elements, toxic organic pollutants, and pathogens to the environment. In this chapter, a broad approach on sewage sludge generation as well as modern treatments, disposal strategies, and adequate management practices at a global level will be addressed to properly educate the public population concerned with the use of this residue and to introduce the book contents. Currently, SSs are mostly landfilled or amended to soils, but they can also be incinerated or used in construction. Therefore, an overview of SS treatments, reuse, and disposal strategies is fundamental to guaranteed maintenance of ecosystem sustainability. Sewage sludge land application and its chemical and microbiological composition, as well as legislation, risk assessment, and methodological aspects related to its characterization, will also be addressed in this book trying to show their advantages and disadvantages. As would be expected, it will allow to review current science on sewage sludge management and to assure environmental sustainability.

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Jussara Borges Regitano, Mayra Maniero Rodrigues and Guilherme Lucio Martins contributed equally with all other contributors.

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Department of Soil Science, “Luiz de Queiroz” College of Agriculture, University of São Paulo, Piracicaba, Brazil

Jussara Borges Regitano, Mayra Maniero Rodrigues, Guilherme Lucio Martins, Júlio Flávio Osti, Douglas Gomes Viana & Adijailton José de Souza

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Ajar Nath Yadav

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Department Soil Science and Agricultural Chemistry, Banaras Hindu University, Varanasi, India

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Regitano, J.B., Rodrigues, M.M., Martins, G.L., Osti, J.F., Viana, D.G., de Souza, A.J. (2022). Sewage Sludge Management for Environmental Sustainability: An Introduction. In: Rajput, V.D., Yadav, A.N., Jatav, H.S., Singh, S.K., Minkina, T. (eds) Sustainable Management and Utilization of Sewage Sludge. Springer, Cham. https://doi.org/10.1007/978-3-030-85226-9_1

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Tertiary wastewater treatment technologies: a review of technical, economic, and life cycle aspects.

literature review on sewage sludge

1. Introduction

2. tertiary wastewater treatment technologies, 2.1. chlorination, 2.2. ultraviolet irradiation, 2.3. membrane filtration, 2.4. constructed wetlands, 2.5. microalgae, 2.6. ozonation, 2.7. photo-fenton, 3. benchmarking of tertiary wastewater treatment technologies, 4. conclusions, author contributions, institutional review board statement, data availability statement, conflicts of interest, abbreviations.

AO52acid orange 52
AOPsadvance oxidation processes
ARBanaerobic resistant bacteria
ARGantibiotic resistance genes
BODbiochemical oxygen demand
BRbiofilm reactor
CODchemical oxygen demand
CWconstructed wetlands
ECemerging contaminants
GHGgreenhouse gases
GOgraphene oxide
HFCWhorizontal flow constructed wetlands
HRAPhigh-rate algal pond
HRPhigh-rate pond
HSSFhorizontal subsurface flow
LCClife cycle costing
MFmicrofiltration
MFCsmicrobial fuel cells
MWCNTsmulti-walled carbon nanotubes
NFnanofiltration
PBRphotobioreactor
PVDFpolyvinylidene fluoride
ROreverse osmosis
SBRsequencing batch reactor
SPFsolar photo-Fenton
TOCtotal organic carbon
UFultrafiltration
UVultraviolet
VFCWvertical flow constructed wetlands
Process InformationTechnicalEconomic
(Cost EUR/m )
Life Cycle
(kg CO eq./m )
Ref.
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
Sulfamethoxazole 220 ng/L 73 [ ]
Ciprofloxacin 153 ng/L 66 [ ]
Norfloxacin 92 ng/L 50 [ ]
Tetracycline 86 ng/L 39 [ ]
Trimethoprim 155 ng/L 65 [ ]
Erythromycin 273 ng/L 43 [ ]
Diclofenac 40 μg/L 97 [ ]
Ibuprofen 40 μg/L 0 [ ]
Clofibric acid 40 μg/L 5 [ ]
Naproxen 40 μg/L 11 [ ]
Gemfibrozil 40 μg/L 45 [ ]
Mefenamic acid 40 μg/L 12 [ ]
E. coli 3.7 Log CFU/100 mL2.5 [ ]
E. coli 4.34 Log CFU/100 mL2.57 [ ]
Enterococci 3.46 Log CFU/100 mL1.18 [ ]
Fecal coliforms 4.57 Log CFU/100 mL2.34 [ ]
F-specific coliphage 2.33 Log CFU/100 mL0.71 [ ]
Somatic coliphage 3.92 Log CFU/100 mL1.68 [ ]
Adenovirus 0.97 Log CFU/100 mL0.81 [ ]
Norovirus 0.74 Log CFU/100 mL0.74 [ ]
Coliforms 4 Log CFU/100 mL4 [ ]
Antib. Resist. Genes 6 Log1.97 [ ]
E. coli 7 Log CFU/mL5 [ ]
0.0003 [ ]
0.005 [ ]
0.006 [ ]
0.046[ ]
0.007[ ]
0.004[ ]
Process InformationTechnicalEconomic
(Cost EUR/m )
Life Cycle
(kg CO eq./m )
Ref.
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
E. coli 5 × 10 CFU/100 mL4 [ ]
E. coli 7.7 Log × 10 CFU/L3.82 [ ]
Enterococci 8.56 Log × 10 CFU/L3.38 [ ]
Fecal coliforms 8.26 Log × 10 CFU/L3.89 [ ]
F-specific coliphage 6.4 Log × 10 CFU/L1.17 [ ]
Somatic coliphage 7.36 Log × 10 CFU/L2.98 [ ]
Adenovirus 2.73 Log gc/L0.24 [ ]
Coliforms 5 Log CFU/mL4 [ ]
Antib. Resist. Genes 6 Log1 [ ]
Antib. Resist. Genes 5 Log copies/L2.5 [ ]
E. coli 2 × 10 CFU/mL5.1 [ ]
Sulfamethoxazole 250 ng/L 100 [ ]
Trimethoprim 90 ng/L 100 [ ]
Erythromycin 200 ng/L 100 [ ]
Acetaminophen 0.1 mM, caffeine 0.12 mM, antipyrine 0.05 mM, doxycycline 0.03 mM, ketorolac 0.05 mM 100 [ ]
Atrazine diuron, alachlor, pentachlorophenol 1 mg/L 72 [ ]
Boldenone 6.57 μM 98 [ ]
BPA 60 μM 22 [ ]
Butylparaben 8 × 10 M 97 [ ]
Carbamazepine 3 μΜ 52 [ ]
Chlorfenvinphos 91 [ ]
Ciprofloxacin 99 [ ]
Chloromycetin 10 mg/L 80 [ ]
Clofibric acid 10 mg/L 98 [ ]
Cyclophosphamide 10 μg/L 28 [ ]
Cytarabine 10 mg/L 10 [ ]
Diatrizoate 50 μM 97 [ ]
Diclofenac 20 mg/L 74 [ ]
Diphenhydramine 5 μM 26 [ ]
Doxycycline 5 × 10 M 27 [ ]
E1 20 mg/L 69 [ ]
E2 20 mg/L 59 [ ]
EE2 37 [ ]
Hydrochlorothiazide 1 μM 59 [ ]
Ibuprofen 10 M 74 [ ]
Iopromide 53 [ ]
Iohexol 3 μΜ 12 [ ]
Irinotecan 10 µg/L 18 [ ]
Isoproturon 1 mg/L 12 [ ]
Ketoprofen 50 µM 99 [ ]
Mefenamic acid 5.5 Log M 56 [ ]
Melatonin 20 mg/L 32 [ ]
Metoprolol 5 × 10 M 69 [ ]
Metronidazole 6 μM 55 [ ]
Naproxen 3 μM 65 [ ]
NDMA 1 mM 100 [ ]
Norfloxacin 5 × 10 M 55 [ ]
Oxtetracycline 93 [ ]
Phenazone 5 μM 96 [ ]
Phenytion 5 μM 88 [ ]
Primidone 50 µM 9 [ ]
Propranolol 100 mg/L 61 [ ]
Sulfadimethoxine 3.2 mM 99 [ ]
Sulfamethoxazole 10 mg/L 83 [ ]
Tamoxifen 10 µg/L 43 [ ]
TCE 8.14 × 10 mol/L 95 [ ]
Tibetene 0.03 mM 87 [ ]
Bezafibrate 112 ng/L 0 [ ]
Metformin 1736 ng/L 27 [ ]
Carbamazepine 333 ng/L 48 [ ]
Gabapentin 1508 ng/L 0 [ ]
Diclofenac 925 ng/L 96 [ ]
Ketoprofen 40 ng/L 97 [ ]
Naproxen 372 ng/L 70 [ ]
Primidone 65 ng/L 3 [ ]
Atenolol 320 ng/L 0 [ ]
Metoprolol 255 ng/L 0 [ ]
Ciprofloxacin 72 ng/L 56 [ ]
Clarithromycin 187 ng/L 10 [ ]
Sulfamethoxazole 355 ng/L 3 [ ]
Trimethoprim 31 ng/L 0 [ ]
Iohexol 4313 ng/L 16 [ ]
Iomeprol 5806 ng/L 0 [ ]
Benzotriazole 6736 ng/L 18 [ ]
Atrazin 25 ng/L 58 [ ]
Isoproturon 4 ng/L 0 [ ]
Mecoprop 365 ng/L 0 [ ]
Terbutryn 23 ng/L 39 [ ]
0.00001 [ ]
0.00644 [ ]
0.0063 [ ]
0.013[ ]
0.026[ ]
0.22[ ]
Process InformationTechnical AspectEconomic Aspect
(Cost EUR/m )
Life Cycle
(kg CO eq./m )
Ref.
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
UF enterococcus 1.87 × 10 CFU/100 mL5 [ ]
UF other coliforms 5.05 × 10 CFU/100 mL2 [ ]
UF N 3.62 mg/L 10 [ ]
UF P 1.86 mg/L 9 [ ]
UF K 16.15 mg/L 0 [ ]
NF-90 2 μg/L 73 [ ]
NF-200 neutral PhACs 65 μg/L 70 [ ]
NF-200 ionic PhACs 65 μg/L 94 [ ]
NF-90 neutral 65 μg/L 97 [ ]
NF-90 ionic 65 μg/L 99 [ ]
NF-90 65 μg/L 73 [ ]
UF 2000 0.5 mg/L 70 [ ]
UF-NF90 750 μg/L 50 [ ]
NF 270 RO 2 μg/L 95 [ ]
NF 150-RO 100 ng/L 95 [ ]
NF 200 100 ng/L 80 [ ]
UF 8000-NF 600 10 ng/L 60 [ ]
UF 8000 10 ng/L 30 [ ]
NF 90-RO 10 mg/L 99 [ ]
NF 200 21 ng/L 100 [ ]
NF 270 10 mg L 60 [ ]
NF270 800 μg/L 58 [ ]
NF90 750 μg/L 97 [ ]
RO 0.55 mg/L 100 [ ]
NF90 10 mg/L 90 [ ]
NF270 10 mg/L 61 [ ]
NF90 0.5 mg/L 98 [ ]
NF270 0.5 mg/L 71 [ ]
RO 0.5 mg/L 89 [ ]
NF90 5400 μg/L 77 [ ]
NF270 5400 μg/L 58 [ ]
RO 5400 μg/L 93 [ ]
UF-Atenolol 778 ng/L 0 [ ]
UF-Bezafibrate 208 ng/L 21 [ ]
UF-Caffeine 17,725 ng/L 0 [ ]
UF-Fenofibric acid 139 ng/L 0 [ ]
UF-Furosemide 1302 ng/L 17 [ ]
UF-Gemfibrozil 18,504 ng/L 71 [ ]
UF-Hydrochlorothiazide 16,628 ng/L 90 [ ]
UF-Ibuprofen 2514 ng/L 1 [ ]
UF-4-AAA 7364 ng/L 0 [ ]
UF-Naproxen 2672 ng/L 12 [ ]
UF-Nicotine 10,954 ng/L 63 [ ]
UF-Ofloxacin 94 ng/L 0 [ ]
RO-Atenolol 1044 ng/L 100 [ ]
RO-Bezafibrate 164 ng/L 100 [ ]
RO-Caffeine 6288 ng/L 99 [ ]
RO-Fenofibric acid 194 ng/L 100 [ ]
RO-Furosemide 811 ng/L 100 [ ]
RO-Gemfibrozil 1035 ng/L 99 [ ]
RO-Hydrochlorothiazide 239 ng/L 95 [ ]
RO-Ibuprofen 574 ng/L 97 [ ]
RO-4-AAA 4472 ng/L 99 [ ]
RO-Naproxen 2583 ng/L 98 [ ]
RO-Nicotine 75 ng/L 76 [ ]
RO-Ofloxacin 87 ng/L 95 [ ]
Including RO 0.46 [ ]
FO-NF 0.96 [ ]
UF-RO 0.4 [ ]
UF 0.45 [ ]
UF-RO 0.8 [ ]
UF-RO 2.32[ ]
NF 0.2[ ]
UF 0.25[ ]
UF 0.40[ ]
MF-RO 0.89[ ]
UF-RO 0.91[ ]
Process InformationTechnical AspectEconomic Aspect
(Cost EUR/m )
Life Cycle
(kg CO eq./m )
Ref.
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
16 s rDNA, intI1, and tet genes1.78 [ ]
14 antibiotic resistance genes0.50 [ ]
ARGs 8–9 Log of copies/mL0.49 [ ]
N 23.4 mg/L 5 [ ]
P 0.2 mg/L 0 [ ]
N 29.3 mg/L 35 [ ]
P 0.2 mg/L 50 [ ]
N 17.3 mg/L 39 [ ]
P 0.2 mg/L 50 [ ]
N 1.39 mg/L 66 [ ]
P 3 mg/L 46 [ ]
N 84.4 mg/L 63 [ ]
P 28.2 mg/L 92 [ ]
N 35 mg/L 46 [ ]
N 72 mg/L 99 [ ]
P 11.7 mg/L 97 [ ]
65 pharmaceuticals 4.3 μg/L 64 [ ]
55 pharmaceuticals 300 ng/L 43 [ ]
53 pharmaceuticals 50 [ ]
56 pharmaceuticals 190 ng/L 32 [ ]
6 pharmaceuticals 7.6–150 μg/L 93 [ ]
Antibiotics 300 ng/L 58 [ ]
Pharmaceuticals 50–200 ng/L 59 [ ]
1.224 [ ]
0.729 [ ]
0.4 [ ]
0.129[ ]
0.432[ ]
0.646[ ]
0.911[ ]
0.5[ ]
0.26[ ]
0.7[ ]
Process InformationTechnicalEconomic
(Cost EUR/m )
Life Cycle
(kg CO eq./m )
Ref.
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
N 40 mg/L 55 [ ]
P 80 mg/L 15 [ ]
N 52 mg/L 82 [ ]
P 8.5 mg/L 95 [ ]
N 18 mg/L 100 [ ]
P 1.4 mg/L 84 [ ]
N 46 mg/L 94 [ ]
P 5.5 mg/L 95 [ ]
Metronidazole 5 μM 100 [ ]
Florfenicol 46 mg/L 97 [ ]
Enrofloxacin 1 mg/L 23 [ ]
Tetracycline 100 μg/L 99 [ ]
Methyl parathion 20 mg/L 80 [ ]
Trimethoprim, Sulfamethoxazole, Triclosan 1.6 ng/L, 360 ng/L, 8 ng/L 44 [ ]
7-amino cephalosporanic acid 100 mg/L 70 [ ]
Cefradine 100 mg/L 94 [ ]
β-estradiol 93 [ ]
17 α-estradiol, 17 β-estradiol, Estrone, Estriol 5 μg/L 90 [ ]
Sulfathiazole, Sulfapyridine, Sulfamethazine, Sulfamethoxazole, Tetracycline, Oxytetracycline 200 μg/L 47 [ ]
Norfloxacin mg/L 37 [ ]
0.42 [ ]
0.162 [ ]
0.6[ ]
0.336[ ]
Process InformationTechnicalEconomic
(Cost EUR/m )
Life Cycle
(kg CO eq./m )
Ref.
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
Coliforms 4 Log CFU/100 mL4 [ ]
Coliforms 5 Log MPN/100 mL2.5 [ ]
Coliforms 5 Log MPN/100 mL2.2 [ ]
Coliforms 7 Log MPN/100 mL4.8 [ ]
E. coli 7.3 Log CFU/mL5.3 [ ]
E. coli 4 Log CFU/mL2.2 [ ]
Salmonella 2.9 Log CFU/mL2.2 [ ]
Enterococcus 3 Log CFU/mL2.2 [ ]
Carbamazepine 75 [ ]
Alachlor 20 [ ]
Bisphenol A 60 [ ]
Atrazine 5 [ ]
Pentachlorophenol 35 [ ]
17-α thinylestradiol 80 [ ]
Carbamazepine 1 μg/L 100 [ ]
Naproxen 1 μg/L 100 [ ]
Beclomethasone 1 μg/L 70 [ ]
Memantine 1 μg/L 80 [ ]
0.03 [ ]
0.03 [ ]
0.025[ ]
0.25[ ]
0.3[ ]
0.3[ ]
Process InformationTechnicalEconomic
(Cost EUR/m )
Life Cycle
(kg CO eq./m )
Ref.
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
S. aureus 6 Log CFU/mL6 [ ]
MRSA ATCC 29213 6 Log CFU/mL6 [ ]
E. coli 6 Log CFU/mL6 [ ]
K. pneumoniae 6 Log CFU/mL6 [ ]
MSSA 1112 6 Log CFU/mL6 [ ]
MSSA 1112 RifR 6 Log CFU/mL6 [ ]
MSSA 1112 CipR 6 Log CFU/mL6 [ ]
MSSA 133 6 Log CFU/mL6 [ ]
MSSA 133 CipR 6 Log CFU/mL6 [ ]
MRSA PC1 6 Log CFU/mL6 [ ]
VISA PC# 6 Log CFU/mL6 [ ]
E. coli 4 Log CFU/mL1 [ ]
Salmonella 2.9 Log CFU/mL2 [ ]
Enterococcus 3 Log CFU/mL0 [ ]
Sulfamethazine 50 mg/L 100 [ ]
Amoxicillin 50 mg/L 100 [ ]
Bezafibrate 112 ng/L 0 [ ]
Gemfibrozil 9 ng/L 96 [ ]
Metformin 1736 ng/L 63 [ ]
Carbamazepine 333 ng/L 94 [ ]
Gabapentin 1508 ng/L 77 [ ]
Diclofenac 925 ng/L 100 [ ]
Ketoprofen 40 ng/L 97 [ ]
Naproxen372 ng/L 97 [ ]
Primidone 65 ng/L 77 [ ]
Atenolol 320 ng/L 87 [ ]
Metoprolol 255 ng/L 90 [ ]
Ciprofloxacin 72 ng/L 61 [ ]
Clarithromycin 187 ng/L 76 [ ]
Sulfamethoxazole 355 ng/L 82 [ ]
Trimethoprim 31 ng/L 88 [ ]
Iohexol 4313 ng/L 94 [ ]
Iomeprol 5806 ng/L 87 [ ]
Benzotriazole 6736 ng/L 95 [ ]
Atrazin 25 ng/L 82 [ ]
Isoproturon 4 ng/L 32 [ ]
Mecoprop 365 ng/L 93 [ ]
Terbutryn 23 ng/L 83 [ ]
Ofloxacin 110 μg/L 100 [ ]
Carbamazepine130 μg/L 96 [ ]
Flumequine 145 μg/L 98 [ ]
Ibuprofen 130 μg/L 95 [ ]
Sulfamethoxazole 140 μg/L 90 [ ]
0.25 [ ]
0.56 [ ]
0.331[ ]
0.554[ ]
0.762[ ]
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Click here to enlarge figure

CategoryTreatment MethodTechnicalEconomic
(Cost EUR/m )
Life Cycle
(kg CO eq. m )
Microbial
(Log Reduction)
Nutrients
(% Reduction)
Pharmaceuticals
(% Reduction)
PhysicochemicalChlorination2.140420.0040.040
UV2.920530.0040.086
Membrane filtration3.506700.6140.754
BiologicalConstructed wetlands0.8753570.7840.511
Microalgae0.0077730.2910.468
Advanced oxidationOzonation3.180630.0300.219
Photo-Fenton4.930840.4050.549
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Zagklis, D.P.; Bampos, G. Tertiary Wastewater Treatment Technologies: A Review of Technical, Economic, and Life Cycle Aspects. Processes 2022 , 10 , 2304. https://doi.org/10.3390/pr10112304

Zagklis DP, Bampos G. Tertiary Wastewater Treatment Technologies: A Review of Technical, Economic, and Life Cycle Aspects. Processes . 2022; 10(11):2304. https://doi.org/10.3390/pr10112304

Zagklis, Dimitris P., and Georgios Bampos. 2022. "Tertiary Wastewater Treatment Technologies: A Review of Technical, Economic, and Life Cycle Aspects" Processes 10, no. 11: 2304. https://doi.org/10.3390/pr10112304

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