Next Article in Journal
Diffusing Environmental Management Practices within the Firm: The Role of Information Provision
Next Article in Special Issue
Sustainability of Egyptian Cities through Utilizing Sewage and Sludge in Softscaping and Biogas Production
Previous Article in Journal
Research on Mechanical Behavior and Energy Evolution of Coal and Rocks with Different Thin Spray-On Liners Thickness under Uniaxial Compressive Loading
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Review

The Influence of Municipal Wastewater Treatment Technologies on the Biological Stabilization of Sewage Sludge: A Systematic Review

by
José Luis Cárdenas-Talero
1,
Jorge Antonio Silva-Leal
2,*,
Andrea Pérez-Vidal
2 and
Patricia Torres-Lozada
1
1
Faculty of Engineering, Study and Control of Environmental Pollution Research Group-ECCA, Universidad del Valle, Cali 760032, Colombia
2
Faculty of Engineering, Electronic, Industrial and Environmental Engineering Research Group-GIEIAM, Universidad Santiago de Cali, Cali 760032, Colombia
*
Author to whom correspondence should be addressed.
Sustainability 2022, 14(10), 5910; https://doi.org/10.3390/su14105910
Submission received: 23 March 2022 / Revised: 29 April 2022 / Accepted: 3 May 2022 / Published: 13 May 2022
(This article belongs to the Special Issue Sludge: A Renewable Source for Energy and Resources Recovery)

Abstract

:
Various wastewater treatment technologies are available today and biological processes are predominantly used in these technologies. Increasing wastewater treatment systems produces large amounts of sewage sludge with variable quantities and qualities, which must be properly managed. Anaerobic and aerobic digestion and composting are major strategies to treat this sludge. The main indicators of biological stabilization are volatile fatty acids (VFAs), volatile solids (VS), the carbon/nitrogen (C/N) ratio, humic substances (HS), the total organic carbon (TOC), the carbon dioxide (CO2) evolution rate, the specific oxygen uptake rate (SOUR), and the Dewar test; however, different criteria exist for the same indicators. Although there is no consensus for defining the stability of sewage sludge (biosolids) in the research and regulations reviewed, controlling the biological degradation, vector attraction, and odor determines the biological stabilization of sewage sludge. Because pollutants and pathogens are not completely removed in biological stabilization processes, further treatments to improve the quality of biosolids and to ensure their safe use should be explored.

1. Introduction

The increasing population will increase municipal wastewater (MWW) generation, and existing sanitation strategies should focus on increasing the wastewater treatment coverage by selecting appropriate treatment technologies based on local conditions [1,2]. On average, although 70% of the MWW generated in high-income countries is treated, only 38%, 28%, and 8% are treated in middle-, middle–low-, and low-income countries, respectively [3,4].
Zhang et al. [5] and Collivignarelli et al. [6] showed that the characteristics of sewage sludge, such as the solid concentration, organic matter (OM), nutrients, heavy metals, and pathogens, vary depending on the following parameters:
(i)
The characteristics of the wastewater (e.g., the biochemical oxygen demand—BOD5, the chemical oxygen demand—COD, and the total suspended solid—TSS).
(ii)
The type of the wastewater collection system (e.g., a sanitary sewer, storm water, or combined systems).
(iii)
The type (e.g., biological or chemical) and stage (i.e., primary, secondary, or mixed) of the wastewater treatment process from which the sludge originates.
(iv)
The sludge stabilization processes (e.g., anaerobic and aerobic digestion, composting, and chemical and thermal treatment).
(v)
The operation conditions, wastewater treatment, and sludge stabilization processes (e.g., the temperature and the sludge retention time).
According to UN-Habitat [7] and Wijesekara et al. [8], the worldwide annual production of sewage sludge was estimated to be 100 million tons (Mt) in 2017 and is projected to reach 175 Mt by 2050.
The final disposal is an important aspect in sewage sludge management because it can affect the environment (e.g., greenhouse gas emissions or the accumulation of heavy metals in soil), economy (e.g., transportation costs and the area requirement in the final disposal), and society (e.g., public acceptance, land occupation, and public health) [8,9] differently.
For promoting the safe management of sewage sludge, the impact of the treatment’s operating conditions, the properties of the MWW on the sludge’s characteristics, and the efficiency of the stabilization processes according to the regulations of each country or region must be evaluated to identify the potential use of sludge [10,11].
The stabilization degree of the sewage sludge achieved can be identified by specific bacteria promoting the biodegradability of OM (biological stabilization), the chemical oxidation of OM (chemical stabilization), and the effect of heat stabilizing the volatile fraction (thermal stabilization) [12,13,14]. Biological processes constitute the most used strategy for sludge stabilization worldwide [15]. About the microbiological and parasitological quality, further treatments (hygienization) reduce the presence of pathogens in biosolids to ensure safe practices for reusing biosolids in agriculture [16,17]. Currently, several studies have revealed the detection of particles of SARS-CoV-2 in MWW and sewage sludge during the pandemic (COVID-19) [18,19].
The terms sewage sludge and biosolids are often used interchangeably [20]. Worldwide, the term biosolids indicates a stabilized sewage sludge, which achieves this condition by one or more treatments and meets the regulations for beneficial use [6,12]. The circular economy approach prioritizes implementing biosolids-reuse strategies, such as agricultural use, which promotes the replacement or reduction in using chemical fertilizers, resulting in economic and environmental benefits [21,22,23]. Reusing biosolids in agriculture is the most used disposal option in some countries such as the United Kingdom (79%), Spain (64%), Australia (55%), and the United States (36%) [24,25].
In Latin America, interest in this topic and the potential use of biosolids with a high agricultural vocation has been growing [26]; although systematic review articles discussing the treatment of municipal wastewater [1,2,3,26], processes for sludge treatment [5], and the reuse and assessment of sludge [6,11,15,20,23,25] have been published, this manuscript presents a bibliometric analysis and a comprehensive reflection on the research trends related to the technologies in municipal wastewater treatment plants (WWTPs) and their influence on the biological stabilization of sewage sludge. The different indicators and criteria are analyzed for the biological stability of the reported sludge and their relationship with sewage water treatment technologies, unveiling no consensus in defining sewage sludge (biosolids) stability or any standardized treatment process indicators.

2. Methods

Based on a bibliometric analysis (2001–2021), the sources of information were two databases, i.e., Scopus and SciELO (from international and Latin American contexts, respectively). The keywords and search equation were defined in English, Portuguese, and Spanish using boolean operators (“AND” and “OR”) [27] and were placed between the keywords to perform the search, e.g., (“municipal wastewater” OR “wastewater treatment”) AND (“sewage sludge” AND “biosolids” AND “sludge stabilization” OR “biological stabilization” OR “sludge management”) AND (“regulations” OR “organic matter” OR “vector attraction” OR “stability indices” OR “stability indicator”). Figure 1 shows the stages developed in the methodology according to the preferred reporting items for systematic reviews and meta-analyses (PRISMA) [28].
The information retrieved from the databases included (i) citation information, (ii) the abstract and keywords, and (iii) bibliographical information, including references to each scientific paper [29]. Subsequently, with “.RIS” files of the citations, the software Mendeley-Desktop© (version 1.19.4, Mendeley Ltd., London, UK) was used as a bibliographic manager, where the publications from the databases were unified and the duplication of the articles was identified to facilitate the organization and review of the information in the bibliometric analysis.
With the refined information, the free version of the software RefViz© (trial version 2.1.2, Omni Inc., Kennesaw, GA, USA) was used to review the content of the articles, support theories and concepts, condense the results, and feed the analyzed data; subsequently, a co-occurrence analysis was performed on the keywords, and clusters were formed that presented similarities or proximities, allowing for the compilation and review of the articles [27].
The results were visualized using the software VOSviewer© (version 1.6.18, Centre for Science and Technology Studies of Leiden University, Leiden, The Netherlands), enabling the analysis of the trends in the development of the topic under study with a minimum of 10 co-occurrences between the keywords [30].

3. Results

3.1. Bibliometric Data

The search equation identified 806 related scientific articles. Scopus found the highest number of publications (528) followed by SciELO (278). Figure 2a shows the growth trend of the publications from 2001 to 2021 and according to country. Particularly, in the last five years, 60 to 100 publications have appeared per year.
The trend in the number of publications is related to the evolution of concepts and programs in governments and agencies, such as zero waste, reduction, reuse, and recycling in the first period (2001–2010) and the second period (2011–2021) with the inclusion of the regulations, politics, and sludge management strategies associated with Sustainable Development Goals, proper planning, environmental protection, public health risks, sustainability, recovery, a life cycle analysis, and a circular economy [6,10,11].
Brazil had the highest number of publications (28%), followed by the United States (17%) and China (15%). Figure 2b describes the top 10 countries reporting publications, adding the production per country in the databases (Scopus and Scielo) with the aim of including a Latin American context in the international analysis. In the Latin American context, Colombia ranks second after Brazil, although it only represents 6% of the publications in the period analyzed. In terms of the associated knowledge, environmental, agricultural, biological, and engineering sciences stand out at the international and Latin American levels.
Figure 3 shows the keywords related to the search equation: the main keywords are labeled in a circle, with each circle’s size defining the frequency of the appearance of these words in the analyzed articles; the larger is the circle, the greater the co-occurrence. The color represents the time and the lines represent the links between the keywords. In addition, the distance between two keywords indicates the strength of the relationship; that is, the closer they are, the more connections they have [30].
We found 96 keywords that group research trends into three clusters: Cluster I represents the technologies in municipal wastewater treatment plants (e.g., biological treatments, activated sludge, and bioreactors); Cluster II represents the sewage sludge characteristics (e.g., the OM, pathogens, heavy metals, and nutrients); and Cluster III represents the biological stabilization processes of sewage sludge (e.g., composting, aerobic, and anaerobic digestion). The development of each cluster is given below.
The keywords presenting the highest number of co-occurrences in descending order were wastewater treatment, anaerobic digestion, sewage sludge, activated sludge, and sludge stabilization. Regarding the research trends, some current topics are highlighted, such as a circular economy, waste activated sludge, advanced oxidation processes, organic compounds, and emerging contaminants. Furthermore, interest still arises around other issues such as wastewater and sludge final disposal, biodegradation, heavy metal, and pathogens, which is of great importance in terms of assessing the potential use of treated wastewater, sewage sludge, and biosolids.

3.2. Municipal Wastewater Treatment Plants (WWTPs)

The composition of MWW is associated with the eating habits of the population and their types of industrial, institutional, and commercial activities. The OM present in MWW constitutes proteins (40–50%), fats (5–10%), lipids (5–10%), fibers (5%), and carbohydrates (25–50%). The quantity is related to rapid population growth, urbanization, improved living conditions, and economic development [3,31].
Unit operations (physical) and processes (chemical and biological) have been identified in four stages of treatment: preliminary, primary, secondary, and tertiary or advanced [32]. Regarding the reduction in the OM, the bibliometric analysis identified that biological processes (93%) are the most studied and applied, with 63% of them associated with aerobic and 37% with anaerobic metabolism.
Figure 4 shows the leading technologies in municipal WWTPs used in different countries, which were selected based on bibliographical information published on the two databases accessed, prioritizing the countries identified in Figure 2b. Although the activated sludge system is the most widely used technology in high-income countries, in middle-income countries, stabilization ponds (SP) are the most commonly used technologies because despite the large area requirement, they have advantages such as low costs, operational simplicity, and sludge stabilization [3,26]. They are followed by an upflow anaerobic sludge blanket (UASB) and activated sludge systems. In low-income countries, primary treatment technologies predominate (e.g., septic tanks, Imhoff tanks, and primary sedimentation) [1,4].
In the field of aerobic treatment, activated sludge technology has different modalities, predominantly the conventional activated sludge (CAS), sequential batch reactor (SBR), extended aeration-activated sludge (EAAS), membrane biological reactor, the elimination of the improved biological phosphorus (EBPR), and to a lesser extent, contact stabilization, bed biofilm reactor (MBBR), and oxidation ditches [35,38,40].
The UASB is the most widely used anaerobic system, particularly in middle- and low-income countries with a tropical climate, such as Brazil, India, and Colombia [1,33]. Generally, the post-treatment requirement of these systems in the case of low- and medium-load MWW for non-compliance with the discharge regulation [41,42] has led to the growth of dual technologies (mainly anaerobic followed by aerobic; A/O, A2/O) [37,40,43], which have benefits such as low energy and chemical consumption, a reduced sludge quantity to be disposed, low equipment requirements, high operational simplicity, and sludge stabilization in the same anaerobic phase by avoiding the additional use of the biological stabilization processes of sewage sludge [2,34].
Table 1 shows a comparative analysis of the main characteristics of the biological systems (used for MWW treatment) documented in the articles and identified in 567 of the 806 publications, such as the activated sludge (e.g., CAS, EAAS, and SBR) and anaerobic treatment (e.g., UASB).
The type of treatment system or metabolism employed influences the quantity and quality of the sludge, i.e., it affects the sewage sludge stabilization, and thereby the sludge management (e.g., the costs, technologies, and usage) [42,44]. High SRT (>18 days) systems result in a low quantity of produced sludge and the development of biological stabilization processes in sewage sludge [32,43]; however, although researchers such as Cokgor et al. [45] and Fisher et al. [46] indicate that the biological stabilization of sewage sludge in EAAS or a SBR is sufficient and comparable to anaerobic processes (e.g., UASB), other researchers [47,48] indicate that the sludge produced from EAAS cannot be considered digested or stabilized because of the influence of the temperature and the SRT on the endogenous decay coefficient.

3.3. Sewage Sludge Characteristics

The annual sludge production in the three countries is as follows: (i) Brazil, with 1.5–3.0 million tons (Mt) for 188 million inhabitants and 20–40% produced from MWW treatment (43% with SP and 30% with UASB reactors); (ii) the United States, with approximately 17 Mt for 298 million inhabitants and 60–80% produced from MWW treatment (75% with CAS technology); and (iii) China, with 12 Mt for 1313 million inhabitants and 40–60% produced from MWW treatment (21% with CAS and 31% with dual systems) [7,25,49,50].
In Germany, the annual sludge production is 2.3 Mt, followed by India and South Africa (2.3 Mt and 1.0 Mt, respectively), and the United Kingdom (1.05 Mt) [25]. In Latin American countries, the sludge production is approximately 0.64 Mt in Mexico [36] and 0.37 Mt in Colombia based on the main municipal WWTPs located in Bogotá, Cali, and Medellin [39].
Historically, sewage sludge management has focused on the final disposal practices, such as incineration and landfill disposal on soil or even in the ocean [51]. However, to adopt practical sustainable solutions, the general requirements (e.g., the production and monitoring frequency), the sewage sludge’s physical, chemical, microbiological, and parasitological characteristics, the environmental and operating conditions of the stabilization processes (e.g., the temperature, SRT, and efficiency), and good management practices (e.g., application rates and agricultural use) must be developed and controlled [9,52].
According to Lu et al. [53] and Kumar et al. [20], sewage sludge contains 50% carbohydrates (sugar, starch, and fiber), 20% fat, representing approximately 30–40% OM, a carbon–nitrogen ratio (C/N) of 10–20%, high levels of heavy metal ions (Cu and Zn), and a pH normally between 6.5 and 7.0. The sewage sludge contains the nutrients necessary for developing agricultural crops, such as nitrogen (N: 3–8%) and phosphorus (P: 1.5–3%) in large quantities and potassium (K: 0.1–0.7%), calcium (Ca), and magnesium (Mg) in low quantities, which increases the potential agricultural use [10,25].
In the sewage sludge, the OM content can be quantified indirectly in terms of volatile solids (VS) [14]. This variable depends on the treatment from which the sludge originates; thus, primary sludge has a higher VS content than secondary sludge originating from both aerobic and anaerobic treatment systems due to the degradation of OM in biological reactors [54,55].
Depending on aspects such as urban development, industrial activities, the characteristics of the population, and the sewerage service, sewage sludge may contain several toxic substances, such as heavy metals; thus, their presence must be analyzed because some of these metals are essential in agricultural use (such as Zn and Cu). In large proportions, metals such as Ni and Cd can have toxicity effects in soil, and the low mobility of such metals increases their concentration in the soil [25]. Other metals (i.e., As, Cr, Hg, Mo, Pb, and Se) can cause potential risks to human, animal, and plant health [44,56].
An important aspect associated with the beneficial or toxic effects of the heavy metals present in sewage sludge corresponds to pH because it influences their solubility. Particularly, acidic media can increase the solubility of heavy metals in sludge samples and make them dynamically toxic; thus, a high risk may be associated with the acidic pH range [57]. For pharmaceutical products such as disinfectants, laundry detergents, pesticides, dyes, paints, preservatives, food additives, personal care products, and organic pollutants, concern has increased owing to a risk to public health [24,58,59].
Pathogens present in sewage sludge originate from human feces and directly relate to the diet and health of the population. They can also originate from animal sources, whose excrement is disposed into the sewage system (e.g., dog and cat feces), or through vectors in the sewers, mainly rodents [25]. These microorganisms grouped in bacteria, including fecal coliforms, Escherichia coli, Campylobacter, and Salmonella sp. [14,60] and parasites, including helminth eggs, represent a risk to human health. Their presence is high in low- and middle-income countries [61]. Viruses, another group of pathogens present in sewage sludge, are subjected to the technical capacity of each country for their detection (e.g., enteric viruses) [62].
Recent reports have identified the presence of SARS-CoV-2 genetic material in MWW and sewage sludge and have investigated its elimination in MWW treatment systems [18]. The particles of SARS-CoV-2 in primary and secondary sludge has been identified in the MWW of the United States [63], Turkey [64], and Spain [19]. However, no epidemiological data establishing a direct relationship between sewage sludge and the risk of a SARS-CoV-2 infection are currently available [18,65].

3.4. Biological Stabilization Processes of Sewage Sludge

The sewage sludge line (Figure 5) is an essential component of municipal WWTPs, and all stages of sludge treatment can account for 40−60% of the total operating costs [66].
The thickening reduces the water content of the sludge and increases the density and solid content. Additionally, anaerobic/aerobic digestion (biological stabilization) reduces the OM, vector attraction, and odor; dewatering reduces the remaining moisture content in sewage sludge, facilitating its transport and final disposal. Further treatment (hygienization) eliminates pathogens [6,10,12]. Table 2 summarizes the advantages and limitations of the most common biological stabilization processes and the characteristics of the material generated in each process.
Table 2. Advantages and limitations of biological stabilization processes and characteristics of the sludge generated.
Table 2. Advantages and limitations of biological stabilization processes and characteristics of the sludge generated.
ProcessAdvantagesLimitationsCharacteristics of the Sludge GeneratedReference (s)
Anaerobic digestion
(AnD)
Reduction in the biological degradation (organic matter) and attraction of vectors, pathogens, and odor.
Potential to use the main gas generated (CH4).
High investment costs, relatively slow degradation of organic matter process, high maintenance and qualified operator requirements; the process depends on the temperature and the SRT.
Limited degradation capacity of heavy metals and complex organic compounds.
Excess moisture.
Emission of greenhouse gases if biogas is not used as a source of renewable energy.
Requires dewatering in addition to requiring further treatment (hygienization) to eliminate pathogens and potentiate unrestricted uses in agriculture. [5,32,50,55,68,69]
Aerobic digestion
(AeD)
Rapid reduction in the biological degradation (organic matter) and attraction of vectors, pathogens, and odor.High operating costs, odor formation, high maintenance and qualified operator requirements; the process depends on the temperature and the SRT.
Limited degradation capacity of heavy metals and complex organic compounds.
Excess moisture.
Emission of greenhouse gases.
Requires dewatering in addition to requiring further treatment (hygienization) to eliminate pathogens and potential unrestricted uses in agriculture.[50,55,69]
CompostingReduction in the biological degradation (organic matter) and attraction of vectors.
Significant reduction in pathogens.
Reduction in sludge volume (up to 60% in 20 days)
Complex management by the volume of sludge generated; the process depends on the temperature, lack of availability of microorganisms, and the presence of unstabilized pathogenic materials.
Limited degradation capacity of heavy metals and complex organic compounds. Heavy metals are only transformed into less mobile forms.
Emission of greenhouse gases.
Low moisture material; however, the sewage sludge requires dewatering before the composting process. It produces value-added products in C, N, and P for horticultural, nursery, and landscape uses.[5,50,55,69,70]
The stabilization process primarily results from the OM degradation, which has been physically classified as soluble and particulate and biochemically classified as biodegradable and non-biodegradable. The soluble biodegradable fraction, commonly referred to as a rapidly biodegradable fraction, is related to the compounds that can be directly adsorbed for synthesizing new cellular materials, such as VFAs, simple carbohydrates, amino acids, and alcohols [43,48]. The particulate biodegradable fraction, known to be slowly biodegradable, is related to the macromolecules that must be broken down into simpler forms before being used by microorganisms [71].
According to the United States Environmental Protection Agency (USEPA) [12], the meaning of “stabilized” sludge is not used uniformly, and the reduction in the biological degradation, attraction of vectors, odor, and pathogens determines the stabilization degree of the sewage sludge. Fisher et al. [46] related stabilization to the OM, pathogens, and odor reductions in sewage sludge. In addition to the content of the OM and nutrients, it is recommended to assess the presence of inhibitory substances, such as heavy metals and pathogens, which could negatively influence the ecosystem and public health [68,72].
Selecting the biological stabilization process depends on factors such as the sewage sludge characteristics, intended use, and final disposal conditions [73]. The bibliometric analysis identified that the most commonly used biological processes are anaerobic digestion (AnD; 49%), composting (27%), and aerobic digestion (AeD; 11%). The chemical (7%) and thermal (6%) stabilization are used mainly for the hygienization process.
In the European Union, 50% of municipal WWTPs use AnD as a sewage sludge stabilization strategy, 18% use AeD, and 8% use other chemical and thermal stabilization processes (e.g., lime application and thermal drying), whereas 24% of municipal WWTPs do not perform any stabilization process [15]. In the United States, 45% of municipal WWTPs use AeD processes, 21% use AnD processes, 20% use other chemical and thermal stabilization processes, 4% use composting, and the remaining 10% do not implement a stabilization process [7,74]. In Canada (particularly Ontario), 34% and 16% of municipal WWTPs use AeD and AnD processes, respectively [38].
In countries such as Brazil, China, Colombia, and India, AnD represents 35–40% of municipal WWTPs, whereas AeD and composting are only applied to 5–10% of the total municipal WWTPs, with the remaining not implementing a stabilization process [7,33,55].
The pathogens removal occurs through various mechanisms (e.g., the external energy requirements, cellular decomposition—heterotrophic and autotrophic, endogenous respiration, the death–regeneration of microorganisms, the predation of bacteria by complex microorganisms, and cell lysis due to adverse environmental conditions—pH, toxic compounds, or temperature) [45,48]. Bacteria die in 1 to 3 months; protozoa and helminth eggs survive up to one year in sewage sludge [60] and enteric viruses and somatic phages persist for 9 to 14 months depending on the temperature and stabilization process of the sewage sludge. Martín-Díaz et al. [62] indicate that somatic phages are a more accurate indicator of the fecal contamination load and the risk of enteric viruses.
The exposure time and temperature conditions to achieve a high reduction efficiency of bacteria and viruses are as follows: (i) for AnD, at least 15 days at 35–55 °C or 60 days at 20 °C; (ii) for AeD, 10 days at 50 °C, 40 days at 20 °C, or 60 days at 15 °C; and (iii) for composting, at least 15 days at 55 °C [50,75]. However, these processes show a low reduction efficiency (45%) of protozoa and helminths; further, complementary hygienization processes are necessary for their removal [16,23,72].
In the case of small municipal WWTPs, the main concern of operators is to reduce health and environmental risks in terms of toxicity [66]. The potential toxicity can be assessed using the seed germination index (phytotoxicity), which provides information about the impact of various hazardous substances and allows for the assessment of sensitivity to individual plant species [56]. Phytotoxicity tests are valuable tools to assess the influence of the stabilization degree on seed germination and root elongation; thus, toxicity tests are included in the directives of relevant agencies (e.g., the USEPA, OECD, and ISO) [76,77].
Although the sewage sludge converted in biosolids contains less N, P, and K than commercial fertilizers, they are considered organic fertilizers in agricultural activities owing to their contribution of OM and nutrients [53], and the land application depends on the amount of N provided, which must be transformed from its organic to inorganic form (i.e., mineralization). This practice reduces the long-term environmental pollution caused by N and P accumulation in the case of chemical fertilizer application and would help farmers by lowering the cost of agricultural inputs and increasing the income from crop production [21,22,72]. Rigby et al. [78] reported a mean mineralizable N fraction for biological stabilized sewage sludge: approximately 29.8% organic N for AnD, 47.2% for AeD, and 6.7% for compost.

Indicators Used to Evaluate the Biological Stabilization of Sewage Sludge

The effect of biological stabilization processes on the proportion of the OM, availability of nutrients, and reduction in pathogens in sewage sludge has prompted efforts to understand the efficiency of the implemented processes, thought indicators, stabilization degree according to the regulatory requirements related to the degradation of OM, control of vector attraction and odor, as well as the physical, chemical, microbiological, and parasitological characteristics of sewage sludge [11,12,22,30,69,79].
With relation to the indicators of the biological stabilization of sewage sludge, the bibliometric analysis identified 218 publications (Figure 6).
Volatile fatty acids (VFAs) and VS are the primary indicators used [80,81,82]. The VFAs can provide useful information on the OM content and is a control parameter mainly used in the stability process during AnD [46]; however, it is not the single indicator to describe the stabilization degree of the sewage sludge [83]. In the case of VS, the organic fraction of the total solids (TS) present in the sewage sludge also quantifies the stabilization degree and vector attraction reduction [14,48].
The performance of the stabilization process is assessed using the relationship between volatile and total solids (VS/TS) or the volatile solids reduction (VSR) using the Van Kleeck and mass balance methods. Here, the minimum threshold of VS/TS is ≤60–65% and VSR are regularly used to consider the stabilized sludge of ≥38–40% [12,84,85].
However, different methods and criteria exist for interpreting the same indicator (e.g., VSR) [85]. According to Özdemir et al. [48], evaluating biological stabilization based on VS represents the only indicator of endogenous decomposition, and it is far from accurate or acceptable. It does not consider the effect of different mechanisms and particulate matter fractions in sewage sludge during the stabilization period. Table 3 shows the main indicators recommended for each biological stabilization process (AnD, AeD, and composting).
Table 3. Sewage sludge biological stabilization indicators reported in literature and regulations.
Table 3. Sewage sludge biological stabilization indicators reported in literature and regulations.
Stabilization ProcessIndicatorAdvantages (A) and
Limitations (L)
UnitCriterionReference (s)
Anaerobic (AnD) and aerobic (AeD) digestionVolatile fatty acids (VFAs) *A: Process quality control, safe quality of the end products
L: Complicated operating procedures and applicable for anaerobic digestion only
mg COD/g OM<430[45,86,87,88,89,90,91,92]
Volatile solids (VS)A: Simple testing methods
L: Procedure control and laboratory assembly
% VS/TS<65[45,86,90,93]
≤60[45,85,86,90,94]
% VSR≥38[12,45,52,86,90,93,95,96,97,98,99,100]
≥40[45,74,85,86,90,101,102,103]
Additional VS when it is anaerobically batch-digested in the laboratory (40 days at 30–37 °C) *
Additional VS when it is aerobically batch-digested in the laboratory (30 days at 20 °C) **
A: Indicates process efficiency
L: Complicated operating procedures
% VSR≤15[12,45,52,86,90,95,96,98,99,100]
% VSR≤17[12,45,52,86,90,95,96,98,99,100]
Humic substances (HS) ***A: Indicates ecological value of end products
L: Complicated operating procedures
mg/gVS≥150[45,81,86,90]
Specific oxygen uptake rate (SOUR) **A: Process quality control
L: Complicated operating procedures, applicable for aerobic digestion only, and ignores the value of end products
mg O2/g TS−h≤1.5[12,45,52,86,90,93,95,96,97,98,99,100]
mg O2/g VSS−h≤2.5[83,104]
CompostingVolatile solidsA: Simple testing methods
L: Procedure control
% VSR≥50[45,75,86,90,101,102,103]
Carbon/nitrogen ratio (C/N)A: Simple testing methods
L: End-products quality control
<12[45,86,87,90,105]
Total organic carbon (TOC)A: Simple testing methods and end-products quality control
L: Need delicacy management
%>5[45,86,90]
CO2 evolution rateA: End-products quality control
L: Unreasonable organic degradation rate and ignores the value of end products
mg CO2/g OM−d<2 (Very stable)
2–4 (Stable)
>4 (Unstable)
[45,70,73,86,90]
Specific oxygen uptake rate (SOUR)A: Process quality control
L: Complicated operating procedures, applicable for aerobic digestion only, and ignores the value of end products
mg O2/g VS−d<3 (Very stable)
3–10 (Stable)
>10 (Unstable)
Self−heating (Dewar test)A: Indicates ecological value of end products
L: Applicable for composting only and ignores the value of end products
Dewar index
(∆T °C)
<10 (Very stable)
10–20 (Stable)
>20 (Unstable)
* Applies only to AnD, ** applies only to AeD, *** applies also to composting. TS: total solids, VS: volatile solids, VSR: reduction in volatile solids, ∆T °C: temperature difference.
In terms of the C/N, Nikaeen et al. [87] suggested that a value less than 12 reflects an advanced degree of OM stabilization. In addition to the TOC, a decreasing trend of the C/N with time indicates OM degradation and sludge stabilization. Thus, the C/N should be combined with other analytical tests and indices to characterize the quality of the final product. Because the C/N is not an appropriate stability indicator, its development during the biological stabilization process must be illustrated [68].
Humic substances (HS) and respirometric methods are alternatives to evaluate sewage sludge stabilization. The first are based on biological stabilization processes that degrade simple organic compounds (proteins, polysaccharides, lipids, etc.) and synthesize complex organic compounds (i.e., HS) [81,88].
Respirometric methods measure the biodegradable OM content and sludge stability [90]; O2 consumption and CO2 generation are measured as dominant indices, but the amount of CO2 released from a biological activity is commonly used to estimate stability in co-composting processes with other organic materials [106]. Another respirometric method is SOUR in which microorganisms use O2 while consuming OM (AeD processes). 1.5-mgO2/g TS-h or 2.5-mgO2/g VSS-h values indicate considerable stabilization [104,107,108]. However, it requires a procedure configuration, monitoring, and procedure, including extended experimental periods [83].
The self-heating tests (Dewar test) of the compost can be used to estimate the microbial respiration and remaining OM indirectly. The increase in temperature within the container for several days is related to the microbial activity and stability of the compost [70,106].
Table 4 presents the indicators of biological stabilization in different studies in terms of municipal WWTPs and the biological stabilization processes of sewage sludge. In 57% of the studies listed, the most related stabilization indicators were VFAs, VSR, and VS/TS in the case of stabilization through AnD. In AeD studies (23%), the stabilization indicators are mainly associated with VSR and VS/TS, and in the case of composting (the remaining 20%), the most commonly used criteria were the TOC and C/N. Indicators such as HS, SOUR, and the Dewar test were the least applied to determine biological stabilization in sewage sludge, owing to the requirement of complex procedures in the laboratory [86,87,88].
Moreover, the anaerobic processes, MWW treatments (e.g., UASBs), and sludge digestion (e.g., AnD) generate biologically stabilized sludge according to the indicators VFAs, VSR, VS/TS, HS, TOC, and C/N.
Additional stabilization processes are required for sewage sludge with an SRT of less than 12 days (CAS). A study in CAS systems reported SOUR values of 3–4.5 mgO2/g VS-h, indicating unstabilized sludge, whereas the EAAS and SBR systems with an SRT of >18 days reported values very close to the stabilization of the sludge, i.e., between 0.9 and 2.0 mgO2/g TS-h [83,107].
Tas [90] and Cokgor et al. [45] evaluated sewage sludge samples from CAS + AeD systems with similar initial loads in different climatic periods and reported the values of the VSR and TOC as 44% and 73%, respectively, in summer. In autumn, a VSR of 31% and a TOC of 43%, and in winter, a VSR of 28% and a TOC of 55% were reported. As the temperature decreased, the efficiency decreased in the VSR and TOC, which directly affected the stabilization degree.
Mei et al. [81] analyzed 16 municipal WWTPs that used AnD and composting as biological sludge stabilization processes. The VSR rates varied between 0.5% and 80.2%. The increase in the HS ranged between 19% and 81% in different cases, showing a close relationship between the stabilization processes and sewage sludge characteristics.
Table 4. Summary of the revised information on the indicators of biological stabilization reported in different publications.
Table 4. Summary of the revised information on the indicators of biological stabilization reported in different publications.
Municipal WWTPsSludge TypeStabilization ProcessOperational Variables of the Process *Indicators of Biological Stabilization
T
(°C)
HRT
(h)
SRT
(d)
pHVFAs
(mgCOD/gVS)
VSR
(%)
VS/TS
(%)
C/NHS
(mg/gVS)
TOC
(%)
SOUR
(mgO2/g TS-h)
Dewar Test
(∆T °C)
Reference (s)
AnaerobicSSNA35–4015207.3-46–6042-186–273---[81,109]
SSNA54–5515207.6-3851-146.1---[81,109]
UASBSSNA3524–4818–338.2160–32055–6860−659.0----[50,54,110,111]
CASSSNA--4–8---73–87---3–4.5-[107,111]
CASSMAnaerobic digestion12–22--7.0–7.9-49−52606.1–17-13.8--[50,72,76,112]
SS25–50-5–128–10140–52052------[59,82,113]
AerobicSSComposting---6.4–6.7-50–80--242–334---[82,114]
AnaerobicSSComposting35--7.3–7.6-43.545–4710-2.01.4–1.110–20[80,87,115]
AerobicSSNA---6.5–9.0-56−63448.9–15----[50,70]
EAASSSNA20–252018–307.1–7.8-32–4060–705.4–5.9--0.9–1.5>20[47,48,79,107,116]
SBRSSNA20-24–406.8-34–3860−706.0--1.8–2.0-[76,83,117]
CASSMAerobic digestion20-18–35--26–3165−80----[90,118,119]
AnaerobicSS3520-6.8–6.9--29---<1.5-[120]
CASSSAerobic digestion59–615–15-7.8–8.3--25–37-----[109]
AnaerobicSS35–6520-6.3–6.9-44–24.562–70-----[121]
* They correspond to the sludge stabilization process; however, when the municipal WWTPs do not use this process, the operation variables of the municipal WWTPs are reported. WWTPs: wastewater treatment plants, T: temperature, HRT: hydraulic retention time, SRT: sludge retention time, VS: volatile solids, TS: total solids, SOUR: specific oxygen absorption rate, VFAs: volatile fatty acids, VSR: reduction in volatile solids, TOC: total organic carbon, C/N: carbon/nitrogen ratio, HS: humic substances, SS: secondary sludge, SM: mixed sludge, UASB: upflow anaerobic sludge blanket, CAS: conventional activated sludge, EAAS: extended aeration activated sludge, and SBR: sequential biological reactor.
In addition to the analysis of the biological stability, regulations associated with the control of the vector attraction and odor of the sewage sludge are defined to determine the sludge’s final disposal and use as well as to avoid the propagation of toxic compounds and pathogens in the environment. These regulations vary between countries, but in general, these set the limits for the maximum concentration of heavy metals and pathogens [51,61].
The first known regulation on the subject was the Directive 86/278−EEC of the European Community [24,122], which introduced limits for the quality of sewage sludge to protect public health. Based on this directive, each country in the region has issued a regulation that, in some cases, has provided stricter limit values and included more restrictions, mainly for pathogens and heavy metals [51,68,77]. In other countries, such as Russia, China, New Zealand, and South Africa, guidelines have also been developed to classify sewage sludge to determine its suitability for agricultural use [21,34].
In Latin America, the regulations are mainly based on the Standard for the Management and the Disposal of Sewage Sludge and Biosolids (40CFR Part 503) issued by the USEPA in 1993 [50,123].
Owing to the low pathogen removal efficiencies of the biological stabilization processes, Silva-Leal et al. [16] and Collivignarelli et al. [66] indicated that biosolids obtained from a biological stabilization process (i.e., AeD and AnD) should consider further hygienization or disinfection treatments (e.g., thermal drying and chemical treatment) to take advantage of the biosolids in restrictive uses (e.g., agriculture). Recently, Peccia et al. [63] and Ducoli et al. [17] indicated that for the safe use of biosolids, hygienization is more relevant during the COVID-19 pandemic.

4. Future Perspectives

Sludge management is key as it represents a considerable part of the yearly operative costs in municipal WWTPs. Biological stabilization processes are associated mainly with OM degradation. Likewise, from a regulatory viewpoint, as sludge stability is also related to the reduction in the attraction for vectors, the analysis of all the physical, chemical, microbiologic, and parasitological characteristics associated with the sewage sludge must be guaranteed.
Despite biological sludge stabilization being widely researched, as identified in the 512 reported articles, only 218 of them address the indicators and criteria to pinpoint the degree of stability, thus evidencing legal gaps and the lack of standardized criteria that may serve as a tool for water utility managers. Additionally, there is no consensus among researchers regarding the stabilization of sludge from aerobic systems such as EAAS and SBR. Moreover, it is important to continue researching the influence of operational and environmental factors in the degree of sludge stabilization.
Due to the increasing worldwide production of sludge and the fact that sludge is considered a unique, complex, and dynamic product, it is indispensable to characterize and follow-up on these products for their adequate reuse and/or final disposal. Its management should be including strategies framed in sustainable development and circular economy objectives, which are focused on waste reduction and reuse. Thus, future work development could be steered toward evaluating aspects such as:
(i)
How the implemented MWW treatment technology and sludge stabilization process influence the degree of stabilization and characteristics of the sewage sludge. Different stabilization indicators should be included in the sewage sludge, contributing to the safe use of sewage sludge and biosolids and minimizing the environmental impacts and public health risks.
(ii)
The verification of the need to apply complementary stabilization and hygienization processes that ensure a safe material that complies with regulations, as it is necessary depending on the characteristics of the sewage sludge.
(iii)
The agronomic potential benefits related to the proportion and availability of the nutrients present in the sewage sludge, which must be compared with that of chemical fertilizers.

5. Conclusions

The weather conditions, size and characteristics of the population, the population’s economic, technical, and technological capacities, and the type of municipal wastewater (MWW) collection, transport, and treatment systems exert an important influence on the characteristics of MWW and the quantity/quality of the sewage sludge generated. Further, the characteristics of the sludge are associated with the type of sludge stabilization and/or hygienization processes implemented.
Anaerobic technologies generally produce a stabilized sludge, whereas conventional aerobic technologies (i.e., CAS) require complementary stabilization processes. Some authors suggest that in aerobic systems with SRT values > 18 days, such as in EAAS and SBR, the sludge generated can be considered stable and would not require additional biological stabilization processes. However, the operational conditions of the system influence the sludge stabilization degree; therefore, it is recommended to verify the sewage sludge characteristics and the mechanisms of the biodegradation of organic matter using different stabilization indicators.
The main stabilization indicators are volatile fatty acids (VFAs), volatile solids (VS), the carbon/nitrogen (C/N) ratio, humic substances (HS), the total organic carbon (TOC), the carbon dioxide (CO2) evolution rate, the specific oxygen uptake rate (SOUR), and the Dewar test. However, it is not recommended to evaluate a single stabilization indicator.
The biological stabilization processes, such as anaerobic and aerobic digestions as well as composting, are the most implemented and researched, improving the sewage sludge characteristics and potential agricultural use.

Author Contributions

Conceptualization, J.L.C.-T., J.A.S.-L., A.P.-V. and P.T.-L.; methodology, J.L.C.-T., J.A.S.-L. and P.T.-L.; software, J.L.C.-T.; formal analysis, J.L.C.-T., J.A.S.-L., A.P.-V. and P.T.-L.; writing—original draft preparation, J.L.C.-T., J.A.S.-L., A.P.-V. and P.T.-L.; writing—review and editing, J.L.C.-T., J.A.S.-L., A.P.-V. and P.T.-L. All authors have read and agreed to the published version of the manuscript.

Funding

This research has been funded by the Dirección General de Investigaciones of the Universidad Santiago de Cali under the call No. 01-2021 and 01-2022. This research has also been supported by the Universidad Santiago de Cali and the Universidad del Valle through the Research Project No. 820-621120-1647.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

All data generated or analyzed during this study are within the submitted manuscript.

Acknowledgments

The authors wish to thank the Universidad Santiago de Cali and the Universidad del Valle for their financial support.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Noyola, A.; Padilla, A.; Morgan, J.M.; Güereca, L.P.; Hernández, F. Typology of Municipal Wastewater Treatment Technologies in Latin America. Clean Soil Air Water 2012, 40, 926–932. [Google Scholar] [CrossRef]
  2. Qu, J.; Wang, H.; Wang, K.; Yu, G.; Ke, B.; Yu, H.Q.; Ren, H.; Zheng, X.; Li, J.; Li, W.W.; et al. Municipal wastewater treatment in China: Development history and future perspectives. Front. Environ. Sci. Eng. 2019, 13, 88. [Google Scholar] [CrossRef]
  3. Sato, T.; Qadir, M.; Yamamoto, S.; Endo, T.; Zahoor, A. Global, regional, and country level need for data on wastewater generation, treatment, and use. Agric. Water Manag. 2013, 130, 1–13. [Google Scholar] [CrossRef]
  4. World Bank. The World Bank Data; GDP per Capita, Atlas Method (Current USD). 2019. Available online: https://data.worldbank.org/indicator/NY.GDP.PCAP.CD (accessed on 12 September 2020).
  5. Zhang, Q.; Hu, J.; Lee, D.J.; Chang, Y.; Lee, Y.J. Sludge treatment: Current research trends. Bioresour. Technol. 2017, 243, 1159–1172. [Google Scholar] [CrossRef]
  6. Collivignarelli, M.C.; Canato, M.; Abbà, A.; Carnevale, M. Biosolids: What are the different types of reuse? J. Clean. Prod. 2019, 238, 117844. [Google Scholar] [CrossRef] [Green Version]
  7. United Nations Human Settlements Programme (UN-Habitat). Global Atlas of Excreta, Wastewater Sludge, and Biosolids Management: Moving forward the Sustainable and Welcome Uses of a Global Resource; LeBlanc, R.J., Matthews, P., Richard, R.P., Eds.; United Nations Human Settlements Programme (UN-Habitat): Nairobi, Kenya, 2008; Available online: https://unhabitat.org/global-atlas-of-excreta-wastewater-sludge-and-biosolids-management (accessed on 5 March 2022).
  8. Wijesekara, H.; Bolan, N.S.; Thangavel, R.; Seshadri, B.; Surapaneni, A.; Saint, C.; Hetherington, C.; Matthews, P.; Vithanage, M. The impact of biosolids application on organic carbon and carbon dioxide fluxes in soil. Chemosphere 2017, 189, 565–573. [Google Scholar] [CrossRef]
  9. Ferrans, L.; Tamara, A.; Müller, A.; Hiroshan, H.; Christina, D.; Serena, C. Selecting sustainable sewage sludge reuse options through a systematic assessment framework: Methodology and case study in Latin America. J. Clean. Prod. 2020, 242, 118389. [Google Scholar] [CrossRef]
  10. Kacprzak, M.; Neczaj, E.; Fijałkowski, K.; Grobelak, A.; Grosser, A.; Worwag, M.; Rorat, A.; Brattebo, H.; Almås, Å.; Singh, B.R. Sewage sludge disposal strategies for sustainable development. Environ. Res. 2017, 156, 39–46. [Google Scholar] [CrossRef]
  11. Gherghel, A.; Teodosiu, C.; De Gisi, S. A review on wastewater sludge valorisation and its challenges in the context of circular economy. J. Clean. Prod. 2019, 228, 244–263. [Google Scholar] [CrossRef]
  12. United States Environmental Protection Agency (USEPA). Control of Pathogens and Vector Attraction in Sewage Sludge; United States Environmental Protection Agency (USEPA): Washington, DC, USA, 2003. [CrossRef]
  13. Pedroza, M.M.; Vieira, G.E.G.; Sousa, J.F.; Pickler, A.C.; Leal, A.C.; Milhomen, C.C. Produção e Tratamento de lodo de esgoto—Uma revisão. Rev. Lib. 2010, 16, 89–188. [Google Scholar]
  14. Al-Gheethi, A.A.; Efaq, A.N.; Bala, J.D.; Norli, I.; Abdel-Monem, M.O.; Kadir, M.O. Removal of pathogenic bacteria from sewage-treated effluent and biosolids for agricultural purposes. Appl. Water Sci. 2018, 8, 74. [Google Scholar] [CrossRef] [Green Version]
  15. Chen, H.; Yan, S.H.; Ye, Z.L.; Meng, H.J.; Zhu, Y.G. Utilization of urban sewage sludge: Chinese perspectives. Environ. Sci. Pollut. Res. 2012, 19, 1454–1463. [Google Scholar] [CrossRef] [PubMed]
  16. Silva-Leal, J.; Bedoya, D.; Torres-Lozada, P. Effect of thermal drying and alkaline treatment on the microbiological and chemical characteristics of biosolids from domestic wastewater treatment plants. Química Nova 2013, 36, 207–214. [Google Scholar] [CrossRef] [Green Version]
  17. Ducoli, S.; Zacco, A.; Bontempi, E. Incineration of sewage sludge and recovery of residue ash as building material: A valuable option as a consequence of the COVID-19 pandemic. J. Environ. Manag. 2021, 282, 111966. [Google Scholar] [CrossRef] [PubMed]
  18. Patel, M.; Chaubey, A.K.; Pittman, C.U., Jr.; Mlsna, T.; Mohan, D. Coronavirus (SARS-CoV-2) in the environment: Occurrence, persistence, analysis in aquatic systems and possible management. Sci. Total Environ. 2020, 765, 142698. [Google Scholar] [CrossRef] [PubMed]
  19. Balboa, S.; Mauricio-Iglesias, M.; Rodríguez, S.; Martínez-Lamas, L.; Vasallo, F.J.; Regueiro, B.; Lema, J.M. The fate of SARS-CoV-2 in wastewater treatment plants points out the sludge line as a suitable spot for incidence monitoring. medRxiv 2021, 772, 145268. [Google Scholar]
  20. Kumar, V.; Chopra, A.K.; Kumar, A. A Review on Sewage Sludge (Biosolids) a Resource for Sustainable Agriculture. Arch. Agric. Environ. Sci. 2017, 2, 340–347. [Google Scholar] [CrossRef]
  21. Badza, T.; Tesfamariam, E.H.; Cogger, C.G. Agricultural use suitability assessment and characterization of municipal liquid sludge: Based on South Africa survey. Sci. Total Environ. 2020, 721, 137658. [Google Scholar] [CrossRef]
  22. Silva-Leal, J.; Pérez-Vidal, A.; Torres-Lozada, P. Effect of biosolids on the nitrogen and phosphorus contents of soil used for sugarcane cultivation. Heliyon 2021, 7, e06360. [Google Scholar] [CrossRef]
  23. Kaszycki, P.; Głodniok, M.; Petryszak, P. Towards a bio-based circular economy in organic waste management and wastewater treatment-The Polish perspective. New Biotechnol. 2021, 61, 80–89. [Google Scholar] [CrossRef]
  24. Aparicio, I.; Santos, J.L.; Alonso, E. Limitation of the concentration of organic pollutants in sewage sludge for agricultural purposes: A case study in South Spain. Waste Manag. 2009, 29, 1747–1753. [Google Scholar] [CrossRef] [PubMed]
  25. Sharma, B.; Sarkar, A.; Singh, P.; Singh, R. Agricultural utilization of biosolids: A review on potential effects on soil and plant grown. Waste Manag. 2017, 64, 117–132. [Google Scholar] [CrossRef] [PubMed]
  26. Hernández-Padilla, F.; Margni, M.; Noyola, A.; Guereca-Hernandez, L.; Bulle, C. Assessing wastewater treatment in Latin America and the Caribbean: Enhancing life cycle assessment interpretation by regionalization and impact assessment sensibility. J. Clean. Prod. 2017, 142, 2140–2153. [Google Scholar] [CrossRef]
  27. Moral, J.A.; Herrera, E.; Santisteban, A.; Cobo, M.J. Software tools for conducting bibliometric analysis in science: An up-to-date review. Prof. Inf. 2020, 29, 4. [Google Scholar] [CrossRef] [Green Version]
  28. Shah, S.; Gwee, S.X.W.; Ng, J.Q.X.; Lau, N.; Koh, J.; Koh, J.; Pang, J. Wastewater surveillance to infer COVID-19 transmission: A systematic review. Sci. Total Environ. 2022, 804, 150060. [Google Scholar] [CrossRef]
  29. Troian, A.; Gomes, M.C. A bibliometric analysis on the use of the multicriteria approach to the water resource management. Gest. Prod. 2020, 27, e4761. [Google Scholar] [CrossRef]
  30. Van-Eck, N.; Waltman, L. Software survey: VOSviewer, a computer program for bibliometric mapping. Scientometrics 2010, 84, 523–538. [Google Scholar] [CrossRef] [Green Version]
  31. Luo, Y.; Yao, J.; Wanga, W.; Zheng, M.; Guo, D.; Chen, Y. Efficient municipal wastewater treatment by oxidation ditch process at low temperature: Bacterial community structure in activated sludge. Sci. Total Environ. 2020, 703, 135031. [Google Scholar] [CrossRef]
  32. Wang, Q.; Wei, W.; Gong, Y.; Yu, Q.; Li, Q.; Sun, J.; Yuan, Z. Technologies for reducing sludge production in wastewater treatment plants: State of the art. Sci. Total Environ. 2017, 587–588, 510–521. [Google Scholar] [CrossRef]
  33. Kaur, R.; Wani, S.P.; Singh, A.K.; Lal, K. Wastewater production, treatment and use in India. In Proceedings of the 2nd Regional Workshop on Safe Use of Wastewater in Agriculture, New Delhi, India, 16–18 May 2012. [Google Scholar]
  34. Jin, L.; Zhang, G.; Tian, H. Current state of sewage treatment in China. Water Res. 2014, 66, 85–98. [Google Scholar] [CrossRef]
  35. Rakedjian, B. Implementation of the Urban Wastewater Treatment Directive in France. Directive 91/271/CE. UWWTD Programme Manager for the French Ministry of Environment. 2015. France. Available online: http://businessdocbox.com/Green_Solutions/87789209-Implementation-of-the-urban-wastewater-treatment-directive-in-france.html (accessed on 5 March 2022).
  36. Comisión Nacional del Agua (CONAGUA). Manual de Agua Potable, Alcantarillado y Saneamiento, Diseño de Plantas de Tratamiento de Aguas Residuales Municipales: Tratamiento y Disposición de Lodos; Secretaria de Medio Ambiente y Recursos Naturales; Comisión Nacional del Agua (CONAGUA): Ciudad de México, México, 2015.
  37. Zhang, Q.; Yang, W.; Ngo, H.; Guo, W.; Jin, P.; Dzakpasu, M.; Yang, S.J.; Wang, Q.; Wang, X.C.; Ao, D. Current status of urban wastewater treatment plants in China. Environ. Int. 2016, 92–93, 11–12. [Google Scholar] [CrossRef] [PubMed]
  38. Jin, C.; Archer, G.; Parker, W. Current status of sludge processing and biosolids disposition in Ontario. Resour. Conserv. Recycl. 2018, 137, 21–31. [Google Scholar] [CrossRef]
  39. Superintendencia de Servicios Públicos Domiciliarios (SSPD). Estudio Sectorial de los servicios públicos domiciliarios de Acueducto y Alcantarillado 2020; Superintendencia de Servicios Públicos Domiciliarios (SSPD): Bogotá, Colombia, 2021.
  40. Maltos, R.A.; Holloway, R.W.; Cath, T.Y. Enhancement of activated sludge wastewater treatment with hydraulic selection. Sep. Purif. Technol. 2020, 250, 117214. [Google Scholar] [CrossRef]
  41. Von Sperling, M.; Freire, V.; Chernicharo, C. Performance evaluation of a UASB-activated sludge system treating municipal wastewater. Water Sci. Technol. 2001, 43, 323–328. [Google Scholar] [CrossRef]
  42. Chan, Y.J.; Chong, M.F.; Law, C.L.; Hassell, D.G. A review on anaerobic-aerobic treatment of industrial and municipal wastewater. Chem. Eng. J. 2009, 155, 1–18. [Google Scholar] [CrossRef]
  43. Orhon, D. Evolution of the activated sludge process: The first 50 years. J. Chem. Technol. Biotechnol. 2014, 90, 608–640. [Google Scholar] [CrossRef]
  44. Demirbas, A.; Edris, G.; Alalayah, W.M. Sludge production from municipal wastewater treatment in sewage treatment plant. Energy Sources Part A Recovery Util. Environ. Eff. 2017, 39, 999–1006. [Google Scholar] [CrossRef]
  45. Cokgor, E.U.; Tas, D.O.; Zengin, G.E.; Insel, G. Effect of stabilization on biomass activity. J. Biotechnol. 2012, 157, 547–553. [Google Scholar] [CrossRef]
  46. Fisher, R.M.; Alvarez-Gaitan, J.P.; Stuetz, R.M. Review of the effects of wastewater biosolids stabilization processes on odor emissions. Crit. Rev. Environ. Sci. Technol. 2019, 49, 1515–1586. [Google Scholar] [CrossRef]
  47. Uggetti, E.; Llorens, E.; Pedescoll, A.; Ferrer, I.; Castellnou, R.; García, J. Sludge dewatering and stabilization in drying reed beds: Characterization of thee full-scale systems in Catalonia, Spain. Bioresour. Technol. 2009, 100, 3882–3890. [Google Scholar] [CrossRef]
  48. Özdemir, S.; Çokgör, E.; Insel, G.; Orhon, D. Effect of extended aeration on the fate of particulate components in sludge stabilization. Bioresour. Technol. 2014, 174, 88–94. [Google Scholar] [CrossRef] [PubMed]
  49. Yang, G.; Zhang, G.; Wang, H. Current state of sludge production, management, treatment and disposal in China. Water Res. 2015, 78, 60–73. [Google Scholar] [CrossRef] [PubMed]
  50. Nascimento, A.; de Souza, A.L.; Oliveira, F.C.; Carvalho, A.R.; Viana, D.G.; Regitano, J.B. Chemical attributes of sewage sludges: Relationships to sources and treatments, and implications for sludge usage in agriculture. J. Clean. Prod. 2020, 258, 120746. [Google Scholar] [CrossRef]
  51. Fijalkowski, K.; Rorat, A.; Grobelak, A.; Kacprzak, M.J. The presence of contaminations in sewage sludge-The current situation. J. Environ. Manag. 2017, 203, 1126–1136. [Google Scholar] [CrossRef] [PubMed]
  52. United States Environmental Protection Agency (USEPA). Land Application of Sewage Sludge a Guide for Land Appliers on the Requirements of the Federal Standards for the Use or Disposal of Sewage Sludge; Standard 40 CFR Part 503; United States Environmental Protection Agency (USEPA): Washington, DC, USA, 1994.
  53. Lu, Q.; He, Z.L.; Stoffella, P.J. Land Application of Biosolids in the USA: A Review. Appl. Environ. Soil Sci. 2012, 2012, 201462. [Google Scholar] [CrossRef] [Green Version]
  54. Shao, L.; Wang, T.; Li, T.; Lu, F.; He, P. Comparison of sludge digestion under aerobic and anaerobic conditions with a focus on the degradation of proteins at mesophilic temperature. Bioresour. Technol. 2013, 140, 131–137. [Google Scholar] [CrossRef]
  55. Anjum, M.; Al-Makishah, N.H.; Barakat, M.A. Wastewater sludge stabilization using pre-treatment methods. Process Saf. Environ. Prot. 2016, 102, 615–632. [Google Scholar] [CrossRef]
  56. Walter, I.; Martínez, F.; Cala, V. Heavy metal speciation and phytotoxic effects of thee representative sewage sludges for agricultural uses. Environ. Pollut. 2006, 139, 507–514. [Google Scholar] [CrossRef]
  57. Meghari, A.R.; Omar, R.K. Physicochemical Characterization of Sewage Sludge of Gaza Wastewater Treatment Plant for Agricultural Utilization. IUG J. Nat. Stud. 2017, 25, 72–78. [Google Scholar]
  58. Zuloaga, O.; Navarro, P.; Bizkarguenaga, E.; Iparraguirre, A.; Vallejo, A.; Olivares, M.; Prieto, A. Overview of extraction, clean-up and detection techniques for the determination of organic pollutants in sewage sludge: A review. Anal. Chim. Acta 2012, 736, 7–29. [Google Scholar] [CrossRef]
  59. Markowicz, A.; Bondarczuk, K.; Cycoń, M.; Sułowicz, S. Land application of sewage sludge: Response of soil microbial communities and potential spread of antibiotic resistance. Environ. Pollut. 2021, 271, 116317. [Google Scholar] [CrossRef] [PubMed]
  60. Sidhu, J.P.; Toze, S.G. Human pathogens and their indicators in biosolids: A literature review. Environ. Int. 2009, 35, 187–201. [Google Scholar] [CrossRef] [PubMed]
  61. Da Rocha, M.C.V.; Barés, M.E.; Braga, M.C.B. Quantification of viable helminth eggs in samples of sewage sludge. Water Res. 2016, 103, 245–255. [Google Scholar] [CrossRef] [PubMed]
  62. Martín-Díaz, J.; Lucena, F.; Blanch, A.R.; Jofre, J. Indicator bacteriophages in sludge, biosolids, sediments and soils. Environ. Res. 2020, 182, 109133. [Google Scholar] [CrossRef]
  63. Peccia, J.; Zulli, A.; Brackney, D.E.; Grubaugh, N.D.; Kaplan, E.H.; Casanovas-Massana, A.; Ko, A.I.; Malik, A.A.; Wang, D.; Wang, M.; et al. SARS-CoV-2 RNA concentrations in primary municipal sewage sludge as a leading indicator of COVID-19 outbreak dynamics. medRxiv 2020. [Google Scholar] [CrossRef]
  64. Kocamemi, B.A.; Kurt, H.; Sait, A.; Sarac, F.; Saatci, A.M.; Pakdemirli, B. SARS-CoV-2 detection in Istanbul wastewater treatment plant sludges. medRxiv 2020. [Google Scholar] [CrossRef]
  65. Brisolara, K.F.; Maal-Bared, R.; Reimers, R.S.; Rubin, A.; Sobsey, M.D.; Bastian, R.K.; Gerba, C.; Smith, J.E.; Bibby, K.; Kester, G.; et al. Assessing and Managing SARS-CoV-2 Occupational Health Risk to Workers Handling Residuals and Biosolids. Sci. Total Environ. 2021, 774, 145732. [Google Scholar] [CrossRef]
  66. Collivignarelli, M.C.; Abbà, A.; Benigna, I. The reuse of biosolids on agricultural land: Critical issues and perspective. Water Environ. Res. 2020, 92, 11–25. [Google Scholar] [CrossRef]
  67. National Research Council (NRC). Biosolids Applied to Land: Advancing Standards and Practices; National Academies Press: Washington, DC, USA, 2002; p. 55. [Google Scholar]
  68. Cieślik, B.M.; Namieśnik, J.; Konieczka, P. Review of sewage sludge management: Standards, regulations and analytical methods. J. Clean. Prod. 2015, 90, 1–15. [Google Scholar] [CrossRef]
  69. Semblante, G.U.; Hai, F.I.; Huang, X.; Ball, A.S.; Price, W.E.; Nghiem, L.D. Trace organic contaminants in biosolids: Impact of conventional wastewater and sludge processing technologies and emerging alternatives. J. Hazard. Mater. 2015, 300, 1–17. [Google Scholar] [CrossRef] [Green Version]
  70. Wichuk, K.M.; McCartney, D. Compost stability and maturity evaluationA literature review. Can. J. Civ. Eng. 2010, 37, 1505–1523. [Google Scholar] [CrossRef]
  71. Xiao, K.; Abbt-Braun, G.; Horn, H. Changes in the characteristics of dissolved organic matter during sludge treatment: A critical review. Water Res. 2020, 187, 116441. [Google Scholar] [CrossRef] [PubMed]
  72. Romanos, D.; Nemer, N.; Khairallah, Y.; Abi Saab, M.T. Assessing the quality of sewage sludge as an agricultural soil amendment in Mediterranean hábitats. Int. J. Recycl. Org. Waste Agric. 2019, 8, 377–383. [Google Scholar] [CrossRef] [Green Version]
  73. Bertanza, G.; Baroni, P.; Canato, M. Ranking sewage sludge management strategies by means of Decision Support Systems: A case study. Resour. Conserv. Recycl. 2016, 110, 1–15. [Google Scholar] [CrossRef]
  74. Seiple, T.E.; Coleman, A.M.; Skaggs, R.L. Municipal wastewater sludge as a sustainable bioresource in the United States. J. Environ. Manag. 2017, 197, 673–680. [Google Scholar] [CrossRef] [PubMed]
  75. European Comission. Disposal and Recycling Routes for Sewage Sludge Part 3: Regulatory Report; Disposal and recycling routes for sewage sludge (Vol. 0); European Comission: Luxemburg, 2001; ISBN 92-894-1799-4. [Google Scholar]
  76. Venegas, M.; Leiva, A.; Bay-Schmith, E.; Silva, J.; Vidal, G. Phytotoxicity of biosolids for soil application: Influence of conventional and advanced anaerobic digestion with sequential pre-treatment. Environ. Technol. Innov. 2019, 16, 100445. [Google Scholar] [CrossRef]
  77. Hudcová, H.; Vymazal, J.; Rozkošný, M. Present restrictions of sewage sludge application in agriculture within the European Union. Soil Water Res. 2019, 14, 104–120. [Google Scholar] [CrossRef]
  78. Rigby, H.; Clarke, B.O.; Pritchard, D.L.; Meehan, B.; Beshah, F.; Smith, S.R.; Porter, N. A critical review of nitrogen mineralization in biosolids-amended soil, the associated fertilizer value for crop production and potential for emissions to the environment. Sci. Total Environ. 2016, 541, 1310–1338. [Google Scholar] [CrossRef]
  79. Alvarenga, P.; Mourinha, C.; Farto, M.; Santos, T.; Palma, P.; Sengo, J.; Morais, M.C.; Cunha-Queda, C. Sewage sludge, compost and other representative organic wastes as agricultural soil amendments: Benefits versus limiting factors. Waste Manag. 2015, 40, 44–52. [Google Scholar] [CrossRef]
  80. Albini, E.; Pecorini, I.; Ferrara, G. Evaluation of biological processes performances using different stability indices. Procedia Environ. Sci. Eng. Manag. 2019, 6, 1–10. [Google Scholar]
  81. Mei, X.; Tang, J.; Zhang, Y. Sludge stabilization: Characteristics of the end-products and an alternative evaluative methodology. Waste Manag. 2020, 105, 355–363. [Google Scholar] [CrossRef] [PubMed]
  82. Fang, W.; Zhang, X.; Zhang, P.; Wan, J.; Guo, H.; Ghasimi, D.S.; Morera, X.C.; Zhang, T. Overview of key operation factors and strategies for improving fermentative volatile fatty acid production and product regulation from sewage sludge. J. Environ. Sci. 2020, 87, 93–111. [Google Scholar] [CrossRef] [PubMed]
  83. Parravicini, V.; Smidt, E.; Svardal, K.; Kroiss, H. Evaluating the stabilisation degree of digested sewage sludge: Investigations at four municipal wastewater treatment plants. Water Sci. Technol. 2006, 53, 81–90. [Google Scholar] [CrossRef] [PubMed]
  84. Ramdani, A.; Dold, P.; Déléris, S.; Lamarre, D.; Gadbois, A.; Comeau, Y. Biodegradation of the endogenous residue of activated sludge. Water Res. 2010, 44, 2179–2188. [Google Scholar] [CrossRef] [PubMed]
  85. Braguglia, C.M.; Coors, A.; Gallipoli, A.; Gianico, A.; Guillon, E.; Kunkel, U.; Mascolo, G.; Richter, E.; Ternes, T.A.; Tomei, M.C.; et al. Quality assessment of digested sludges produced by advanced stabilization processes. Environ. Sci. Pollut. Res. 2015, 22, 7216–7235. [Google Scholar] [CrossRef]
  86. Kazmierczak, M. Sewage sludge stabilization indicators in aerobic digestion—A review. Ann. Wars. Univ. Life Sci. SGGW Land Reclam. 2012, 44, 101–109. [Google Scholar] [CrossRef]
  87. Nikaeen, M.; Nafez, A.H.; Bina, B.; Nabavi, B.F.; Hassanzadeh, A. Respiration and enzymatic activities as indicators of stabilization of sewage sludge composting. Waste Manag. 2015, 39, 104–110. [Google Scholar] [CrossRef]
  88. Li, H.; Li, Y.K.; Li, C. Evolution of humic substances during anaerobic sludge digestion. Environ. Eng. Manag. J. 2017, 6, 1577–1582. [Google Scholar] [CrossRef]
  89. British Standard Institution (BSI). Specification for Whole Digestate, Separated Liquor and Separated Fibre Derived from the Anaerobic Digestion of Source-Segregated Biodegradable Materials; PAS 110; British Standard Institution (BSI): London, UK, 2010. [Google Scholar]
  90. Tas, D. Respirometric assessment of aerobic sludge stabilization. Bioresour. Technol. 2010, 101, 2592–2599. [Google Scholar] [CrossRef]
  91. Desarrollo de Sistemas Sostenibles de Producción y Uso de Biogás Agroindustria en España (PROBIOGAS). Guía de Utilización Agrícola de Los Materiales Digeridos por Biometanización; Desarrollo de Sistemas Sostenibles de Producción y Uso de Biogás Agroindustria en España (PROBIOGAS): Murcia España, 2011; ISBN 978-84-694-1868-0. [Google Scholar]
  92. Ministerio de Agricultura Pesca Alimentación y Medio Ambiente. Real Decreto 1310 de 1990-Orden AAA/1072/2013; Ministerio de Agricultura Pesca Alimentación y Medio Ambiente: City, España, 2013.
  93. Conselho Nacional do Meio Ambiente (CONAMA). Resolução N° 498, de 19 de Agosto de 2020. Define Critérios e Procedimentos Para Produção e Aplicação de Biossólido em Solos, e dá Outras Providências; Conselho Nacional do Meio Ambiente (CONAMA): Belo Horizonte, Brasil, 2020.
  94. Ministerio de Vivienda, Construcción y Saneamiento. Decreto Supremo N° 015-2017-Vivienda; Ministerio de Vivienda, Construcción y Saneamiento: Lima, Perú, 2017.
  95. United States Enviromental Protection Agency (USEPA). Standards for the Use or Disposal of Sewage Sludge; 40 CFR Part 503; United States Environmental Protection Agency (USEPA): Washington, DC, USA, 1993.
  96. Secretaría de Medio Ambiente y Recursos Naturales (SERMANAT). Norma de Protección Ambiental de Lodos y Biosólidos. Especificaciones y Límites Máximos Permisibles de Contaminantes Para su Aprovechamiento y Disposición Final; NOM-004-SERMANAT; Secretaría de Medio Ambiente y Recursos Naturales (SERMANAT): Ciudad de México, México, 2002.
  97. New Zealand Water and Wastes Association (NZWWA). Guidelines for the Safe Application of Biosolids to Land in New Zealand; New Zealand Water and Wastes Association (NZWWA): Wellington, New Zealand, 2003; ISBN 1-877134-43-0. [Google Scholar]
  98. Water Research Commission (WRC). Guidelines for the Utilization and Disposal of Wastewater Sludge; Volume 2: Requirements for the Agricultural Use of Wastewater Sludge; Rep. TT 262/06; Water Research Commission (WRC): Pretoria, South Africa, 2006. [Google Scholar]
  99. Canadian Council of Ministers of the Environment (CCME). A Review of the Current Canadian Legislative Framework for Wastewater Biosolids; Canadian Council of Ministers of the Environment (CCME): Winnipeg, MB, Canada, 2010; ISBN 978-1-896997-95-7.
  100. Ministerio de Vivienda, Ciudad y Territorio (MINVIVIENDA). Decreto 1287 del 10 de Julio de 2014; Ministerio de Vivienda, Ciudad y Territorio (MINVIVIENDA): Bogotá, Colombia, 2014.
  101. GB 18918-2002; Discharge Standard of Pollutants for Municipal Wastewater Treatment Plant. Ministry of Environmental Protection of China: Beijing, China, 2003.
  102. CJ/T 510-2017; Standard for Sludge Stabilization Treatment of Municipal Wastewater Treatment Plant. Standards Press of China: Beijing, China, 2017.
  103. GBT 4284-2018; Standards for Pollutant Control of Sludge for Agricultural Use. Standards Press of China: Beijing, China, 2018.
  104. Nowak, O. Sewage sludge stabilisation at treatment plants without mesophilic digestion (in German). Presented at the Ö WAV/TU-Workshop” Sewage sludge”, Vienna University of Technology, 26–27. Vienna Publ. Wien. Mitt. 2002, 177, 29–76. [Google Scholar]
  105. Ministerio de la Presidencia. Real Decreto 506/2013, de 28 de Junio, Sobre Productos Fertilizantes. Boletín Oficial del Estado (BOE) 10 Julio 2013, 164, e51118–e51207, España. Available online: https://www.boe.es/boe/dias/2013/07/10/pdfs/BOE-A-2013-7540.pdf (accessed on 5 March 2022).
  106. Evangelou, A.; Calabrò, P.S.; Greco, R.; Sánchez, A.; Komilis, D. Biodegradation activity of eight organic substrates: A correlation study of different test methods. Waste Biomass Valorization 2016, 7, 1067–1080. [Google Scholar] [CrossRef] [Green Version]
  107. Tonkovic, Z. Aerobic stabilisation criteria for BNR biosolids. Water Sci. Technol. 1999, 39, 167–174. [Google Scholar] [CrossRef]
  108. Li, Z.; Hang, Z.; Zhang, Q.; Zhang, S.; Zhang, T.; Yu, H. Tuning of activated sludge in winter based on respirogram profiles under standard and site temperatures. J. Environ. Sci. 2019, 79, 330–338. [Google Scholar] [CrossRef] [PubMed]
  109. López, A.; Rodríguez-Chueca, J.; Mosteo, R.; Gómez, J.; Ormad, M.P. Microbiological quality of sewage sludge after digestion treatment: A pilot scale case of study. J. Clean. Prod. 2020, 254, 120101. [Google Scholar] [CrossRef]
  110. Terreros-Mecalco, J.; Olmos-Dichara, A.; Noyola-Robles, A.; Ramírez-Vives, F.; Monroy-Hermosillo, O. Digestión anaerobia de lodo primario y secundario en dos reactores UASB en serie. Rev. Mex. Ing. Química 2009, 8, 153–161. [Google Scholar]
  111. Xu, J.; Yuan, H.; Lin, J.; Yuan, W. Evaluation of thermal, thermal-alkaline, alkaline and electrochemical pretreatments on sludge to enhance anaerobic biogas production. J. Taiwan Inst. Chem. Eng. 2013, 45, 2531–2536. [Google Scholar] [CrossRef]
  112. Černe, M.; Palčić, I.; Pasković, I.; Major, N.; Romić, M.; Filipović, V.; Igrc, M.D.; Perčin, A.; Ban, S.G.; Zorko, B.; et al. The effect of stabilization on the utilization of municipal sewage sludge as a soil amendment. Waste Manag. 2019, 94, 27–38. [Google Scholar] [CrossRef]
  113. Xiong, H.; Chen, J.; Wang, H.; Shi, H. Influences of volatile solid concentration, temperature and solid retention time for the hydrolysis of waste activated sludge to recover volatile fatty acids. Bioresour. Technol. 2012, 119, 285–292. [Google Scholar] [CrossRef]
  114. Vaca, R.; Lugo, J.; Martinez, R.; Esteller, M.V.; Zavaleta, H. Effects of sewage sludge and sewage sludge compost amendment on soil properties and Zea mays L. plants (heavy metals, quality and productivity). Rev. Int. Contam. Ambient. 2011, 27, 304–311. [Google Scholar]
  115. Toledo, M.; Gutiérrez, M.C.; Siles, J.A.; Martín, M.A. Full-scale composting of sewage sludge and market waste: Stability monitoring and odor dispersion modeling. Environ. Res. 2018, 167, 739–750. [Google Scholar] [CrossRef] [PubMed]
  116. Park, C.; Abu-Orf, M.M.; Novak, J. The Digestibility of Waste Activated Sludges. Water Environ. Res. 2006, 78, 59–68. [Google Scholar] [CrossRef] [PubMed]
  117. Li, X.; Zhang, R. Aerobic treatment of dairy wastewater with sequencing batch reactor systems. Bioprocess Biosyst. Eng. 2002, 25, 103–109. [Google Scholar] [CrossRef] [PubMed]
  118. Yeneneh, A.; Sen, T.; Chong, S.; Ang, H.M.; Kayaalp, A. Effect of combined microwave-ultrasonic pretreatment on anaerobic biodegradability of primary, excess activated and mixed sludge. Comput. Water Energy Environ. Eng. 2013, 2, 7–11. [Google Scholar] [CrossRef] [Green Version]
  119. Souza, T.S.; Ferreira, L.C.; Sapkaite, I.; Pérez-Elvira, S.I.; Fdz-Polanco, F. Thermal pretreatment and hydraulic retention time in continuous digesters fed with sewage sludge: Assessment using the ADM1. Bioresour. Technol. 2013, 148, 317–324. [Google Scholar] [CrossRef]
  120. Smidt, E.; Parravicini, V. Effect of sewage sludge treatment and additional aerobic post-stabilization revealed by infrared spectroscopy and multivariate data analysis. Bioresour. Technol. 2009, 100, 1775–1780. [Google Scholar] [CrossRef]
  121. Liu, S.; Zhu, N.; Ning, P.; Li, L.Y.; Gong, X. The one-stage autothermal thermophilic aerobic digestion for sewage sludge treatment: Effects of temperature on stabilization process and sludge properties. Chem. Eng. J. 2012, 197, 223–230. [Google Scholar] [CrossRef]
  122. Council of the European Communities (CEC). Directive 86/278/EEC. Protection of the Environment, and in Particular of the Soil, when Sewage Sludge is Used in Agriculture. Off. J. Eur. Communities EUR-Lex 1986, 181, 6–12. [Google Scholar]
  123. Ospina, F.A.; Rodríguez, A.; Gónzalez, J.M. Comparación de la reglamentación para el manejo de lodos provenientes de agua residual en Argentina, Chile y Colombia. Rev. Investig. Agrar. Ambient. 2017, 8, 227–237. [Google Scholar] [CrossRef]
Figure 1. Stages of systematic reviews. Source: adapted from Shah et al. [28].
Figure 1. Stages of systematic reviews. Source: adapted from Shah et al. [28].
Sustainability 14 05910 g001
Figure 2. Number of publications (a) in databases and (b) by country.
Figure 2. Number of publications (a) in databases and (b) by country.
Sustainability 14 05910 g002
Figure 3. Cluster network obtained through the bibliometric mapping of keywords.
Figure 3. Cluster network obtained through the bibliometric mapping of keywords.
Sustainability 14 05910 g003
Figure 4. Main technologies in WWTPs used in different countries. A2/O: anaerobic−anoxic−aerobic; A/O: anaerobic−aerobic; UASB: upflow anaerobic sludge blanket; and other processes: primary treatment (septic tanks, Imhoff tanks, primary sedimentation, etc.). Source: adapted from Noyola et al. [1], Sato et al. [3], the World Bank [4], Pedroza et al. [13], Kaur et al. [33], Jin et al. [34], Rakedjian [35], CONAGUA [36], Zhang et al. [37], Jin et al. [38], SSPD [39], and Maltos et al. [40].
Figure 4. Main technologies in WWTPs used in different countries. A2/O: anaerobic−anoxic−aerobic; A/O: anaerobic−aerobic; UASB: upflow anaerobic sludge blanket; and other processes: primary treatment (septic tanks, Imhoff tanks, primary sedimentation, etc.). Source: adapted from Noyola et al. [1], Sato et al. [3], the World Bank [4], Pedroza et al. [13], Kaur et al. [33], Jin et al. [34], Rakedjian [35], CONAGUA [36], Zhang et al. [37], Jin et al. [38], SSPD [39], and Maltos et al. [40].
Sustainability 14 05910 g004
Figure 5. Sewage sludge treatment alternatives. Source: adapted from Silva-Leal et al. [16], Jin et al. [34], and the NRC [67].
Figure 5. Sewage sludge treatment alternatives. Source: adapted from Silva-Leal et al. [16], Jin et al. [34], and the NRC [67].
Sustainability 14 05910 g005
Figure 6. Main indicators of biological stabilization identified by the bibliometric analysis. VFAs: volatile fatty acids, C: carbon, N: nitrogen, TOC: total organic carbon, CO2: carbon dioxide, and SOUR: specific oxygen absorption rate.
Figure 6. Main indicators of biological stabilization identified by the bibliometric analysis. VFAs: volatile fatty acids, C: carbon, N: nitrogen, TOC: total organic carbon, CO2: carbon dioxide, and SOUR: specific oxygen absorption rate.
Sustainability 14 05910 g006
Table 1. Main characteristics of biological treatment technologies documented in articles.
Table 1. Main characteristics of biological treatment technologies documented in articles.
CharacteristicsCASEAAS–SBRUASB
Kinetics of organic
matter conversion
CnHaObNc + 5O2

CO2 + H2O + NH3 +
biomass
CnHaObNc + 7O2

CO2 + H2O + H+ + NO3 + biomass
CnHaObNc

CH4 + CO2 + H2O + NH3 + biomass
Area requirement (m2/inhabitant)0.2–0.30.25–0.350.1–0.2
Sludge retention time (SRT)4–15 days18–30 days30–40 days
Hydraulic retention time (HRT)5–14 h18–36 h6–14 h
Removal efficiency of COD80–90%90–95%60–70%
Removal efficiency of BOD585–95%80–98%60–80%
Energy requirementsReducedHighLow to moderate
Temperature influenceAverageHighHigh
Biological stabilization of sludgeLow and insufficientSufficientHigh
Complementary biological stabilization processes of sludgeNecessaryNot requiredNot required
Sludge production (L/per*d)High (8.2)Medium (3.3–5.6)Low (0.2–0.6)
COD: chemical oxygen demand; BOD: biological oxygen demand; CAS: activated sludge conventional; SBR: sequential biological reactor; EAAS: extended aeration activated sludge; and UASB: anaerobic upflow reactor with sludge mantle. Source: adapted from Noyola et al. [1], von Sperling et al. [41], and Chan et al. [42].
Publisher’s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Share and Cite

MDPI and ACS Style

Cárdenas-Talero, J.L.; Silva-Leal, J.A.; Pérez-Vidal, A.; Torres-Lozada, P. The Influence of Municipal Wastewater Treatment Technologies on the Biological Stabilization of Sewage Sludge: A Systematic Review. Sustainability 2022, 14, 5910. https://doi.org/10.3390/su14105910

AMA Style

Cárdenas-Talero JL, Silva-Leal JA, Pérez-Vidal A, Torres-Lozada P. The Influence of Municipal Wastewater Treatment Technologies on the Biological Stabilization of Sewage Sludge: A Systematic Review. Sustainability. 2022; 14(10):5910. https://doi.org/10.3390/su14105910

Chicago/Turabian Style

Cárdenas-Talero, José Luis, Jorge Antonio Silva-Leal, Andrea Pérez-Vidal, and Patricia Torres-Lozada. 2022. "The Influence of Municipal Wastewater Treatment Technologies on the Biological Stabilization of Sewage Sludge: A Systematic Review" Sustainability 14, no. 10: 5910. https://doi.org/10.3390/su14105910

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop