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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Chem. Eng.</journal-id>
<journal-title>Frontiers in Chemical Engineering</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Chem. Eng.</abbrev-journal-title>
<issn pub-type="epub">2673-2718</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1129783</article-id>
<article-id pub-id-type="doi">10.3389/fceng.2023.1129783</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Chemical Engineering</subject>
<subj-group>
<subject>Review</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Wastewater and sludge valorisation: a novel approach for treatment and resource recovery to achieve circular economy concept</article-title>
<alt-title alt-title-type="left-running-head">Kathi et al.</alt-title>
<alt-title alt-title-type="right-running-head">
<ext-link ext-link-type="uri" xlink:href="https://doi.org/10.3389/fceng.2023.1129783">10.3389/fceng.2023.1129783</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Kathi</surname>
<given-names>Srujana</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1955156/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Singh</surname>
<given-names>Siril</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2169170/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Yadav</surname>
<given-names>Rajni</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2231873/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Singh</surname>
<given-names>Anand Narain</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/528929/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Mahmoud</surname>
<given-names>Alaa El Din</given-names>
</name>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
<xref ref-type="aff" rid="aff5">
<sup>5</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/906401/overview"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>UGC-Human Resource Development Centre</institution>, <institution>Pondicherry University</institution>, <addr-line>Puducherry</addr-line>, <country>India</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>Department of Environment Studies</institution>, <institution>Panjab University</institution>, <addr-line>Chandigarh</addr-line>, <country>India</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>Soil Ecosystem and Restoration Ecology Lab</institution>, <institution>Department of Botany</institution>, <institution>Panjab University</institution>, <addr-line>Chandigarh</addr-line>, <country>India</country>
</aff>
<aff id="aff4">
<sup>4</sup>
<institution>Environmental Sciences Department</institution>, <institution>Faculty of Science</institution>, <institution>Alexandria University</institution>, <addr-line>Alexandria</addr-line>, <country>Egypt</country>
</aff>
<aff id="aff5">
<sup>5</sup>
<institution>Green Technology Group</institution>, <institution>Faculty of Science</institution>, <institution>Alexandria University</institution>, <addr-line>Alexandria</addr-line>, <country>Egypt</country>
</aff>
<author-notes>
<fn fn-type="edited-by">
<p>
<bold>Edited by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1343031/overview">Surindra Suthar</ext-link>, Doon University, India</p>
</fn>
<fn fn-type="edited-by">
<p>
<bold>Reviewed by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1489426/overview">Daniel Pinto Fernandes</ext-link>, Federal University of Alagoas, Brazil</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/89952/overview">Vinay Kumar Tyagi</ext-link>, National Institute of Hydrology, India</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Anand Narain Singh, <email>dranand1212@gmail.com</email>
</corresp>
</author-notes>
<pub-date pub-type="epub">
<day>27</day>
<month>04</month>
<year>2023</year>
</pub-date>
<pub-date pub-type="collection">
<year>2023</year>
</pub-date>
<volume>5</volume>
<elocation-id>1129783</elocation-id>
<history>
<date date-type="received">
<day>22</day>
<month>12</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>05</day>
<month>04</month>
<year>2023</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2023 Kathi, Singh, Yadav, Singh and Mahmoud.</copyright-statement>
<copyright-year>2023</copyright-year>
<copyright-holder>Kathi, Singh, Yadav, Singh and Mahmoud</copyright-holder>
<license xlink:href="http://creativecommons.org/licenses/by/4.0/">
<p>This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.</p>
</license>
</permissions>
<abstract>
<p>Global demand for freshwater is rapidly escalating. It is highly essential to keep pace with the necessities of the increasing population. The effluents of wastewater are gradually identified as a reservoir of resources for energy generation and economic boom. Henceforth, most wastewater and sludge have great potential for reuse and recycling. The re-utilization and valorization of wastewater and sludge contribute to accomplishing sustainable development goals, combating water scarcity, and alleviating adverse environmental impacts of wastewater on the environmental components. The present article highlights the most novel approaches for wastewater treatment for the waste valorization of different industrial origins and the generation of value-added products and recovery of biopolymers, vitamins, enzymes, dyes, pigments, and phenolic compounds. We highlighted the life cycle assessment and techno-economic analysis. In addition, we have addressed a critical overview of the barriers to the large-scale application of resource recovery strategies and economic, environmental, and social concerns associated with using waste-derived products.</p>
</abstract>
<abstract abstract-type="graphical">
<title>Graphical Abstract</title>
<p>
<graphic xlink:href="FCENG_fceng-2023-1129783_wc_abs.tif" position="anchor"/>
</p>
</abstract>
<kwd-group>
<kwd>resource recovery</kwd>
<kwd>SDG 6</kwd>
<kwd>value-added products</kwd>
<kwd>sustainable development goal</kwd>
<kwd>circular economy</kwd>
<kwd>waste valorization</kwd>
</kwd-group>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Environmental Chemical Engineering</meta-value>
</custom-meta>
</custom-meta-wrap>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>An essential requirement for human civilisation is having access to clean and fresh water. The exploitation of non-renewable natural resources has led to their depletion and raised environmental concerns due to the world&#x2019;s rapid population growth and economic development. Water is one of the natural resources that has been impacted by multiple issues, including poor quality, scarcity, and lack of access to clean water (<xref ref-type="bibr" rid="B177">Scanlon et al., 2023</xref>). The shrinking of freshwater resources has emerged as one of the significant global issues in the twenty-first century faced by the human race. The ability of the planet&#x2019;s natural resources to sustainably meet the rising demand has also grown to be a challenging problem due to population growth, urbanisation, and industrialisation.</p>
<p>In fact, in the 2030 Agenda towards sustainable development goals of the United Nations, the sixth goal was established as a goal for clean water and sanitation to guarantee sanitation and water accessibility and sustainable management worldwide (<xref ref-type="bibr" rid="B126">Mahmoud et al., 2021a</xref>). In the past few years, urbanisation has led to the generation of a considerable amount of solid waste and wastewater effluents disposed of in nearby water bodies without complete treatment (<xref ref-type="bibr" rid="B129">Markandeya and Shukla, 2022</xref>). The release of such wastes and effluents into the environment has many repercussions like eutrophication, groundwater leaching, spreading of pathogens, increase in waterborne diseases, and deterioration of water body aesthetics (<xref ref-type="bibr" rid="B13">Bashir et al., 2020</xref>; <xref ref-type="bibr" rid="B82">Jadon et al., 2022</xref>). The current wastewater treatment plants are now being examined as a potential reservoir of resources for nutrient recovery and the generation of value-added products (<xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>). Previously, these facilities were designed to treat wastewater to meet the essential physical, biological and chemical standards before disposing it into the environment (<xref ref-type="bibr" rid="B22">Bora et al., 2020</xref>). Utilising sewage sludge and wastewater as a source of nutrients and value-added goods is essential for the world&#x2019;s transformation from a linear to a circular economy when resource availability is constrained to lessen the mounting stress on our water resources (<xref ref-type="bibr" rid="B157">Puyol et al., 2017</xref>). High-end wastewater treatment systems and advanced waste management technologies offer multiple ways for nutrient recovery and transformation to value-added products. Establishing a circular resource flow can help the water sector alleviate water scarcity and generate additional revenue (<xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>) (<xref ref-type="fig" rid="F1">Figure 1</xref>).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>The circular economy concept of waste valorisation and resource recovery from wastewater and sludge. Adapted from <xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>, with permission from Elsevier.</p>
</caption>
<graphic xlink:href="fceng-05-1129783-g001.tif"/>
</fig>
<p>Wastewater and sludge, which are now recognised as valuable sources of nutrients like phosphorus and ammonium, contain massive volumes of both organic and inorganic compounds (<xref ref-type="bibr" rid="B131">Meena et al., 2022</xref>). The world&#x2019;s population is increasing, which means that more food needs to be produced. To do this, farmers use fertilisers which contain phosphorous. To make these fertilisers, two substances called ammonium and phosphate are needed. Studies have shown that the demand for these two substances is increasing as more fertilisers are needed. (<xref ref-type="bibr" rid="B204">Tilman et al., 2002</xref>; <xref ref-type="bibr" rid="B69">Gong et al., 2022</xref>).</p>
<p>Partially or untreated wastewater containing excess phosphorous and ammonium released in surface waters may lead to eutrophication and imbalance in the aquatic ecosystem; therefore, removing these nutrients is essential to maintain healthy aquatic life (<xref ref-type="bibr" rid="B51">Diaz et al., 2022</xref>; <xref ref-type="bibr" rid="B56">el-Maghrabi et al., 2022</xref>). Moreover, the depletion of natural phosphorous resources from agroecosystems has become a global issue (<xref ref-type="bibr" rid="B176">Sattari et al., 2012</xref>; <xref ref-type="bibr" rid="B6">Alewell et al., 2020</xref>). Therefore, wastewater and sludge valorisation have multiple benefits of nutrient recovery, generation of value-added products, sustainable wastewater treatment, alleviating water scarcity, additional revenue generation, and reduction in environmental contamination (<xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>).</p>
<p>Conventional wastewater treatment plants and their integrated system are primarily designed to treat wastewater to reduce organic and suspended solid load and meet the basic discharge requirements (<xref ref-type="bibr" rid="B124">Mahmoud and Kathi, 2022</xref>). Traditional physical techniques mainly use various screens, settling tanks and adsorbents with enhanced adsorption efficiency and offer a modest process for wastewater treatment (<xref ref-type="bibr" rid="B89">Kaviya, 2022</xref>). Emerging high-end technologies and advanced membrane systems empowered by hydraulic and osmotic pressure, thermal and electrical systems are promising technologies for enhanced treatment and valorisation, leading to resource recovery and generation of value-added products (<xref ref-type="bibr" rid="B223">Xu et al., 2017</xref>; <xref ref-type="bibr" rid="B163">Ray et al., 2020</xref>). For the oxidative elimination of contaminants, chemical methods utilising radical chemistry and electrochemical technologies based on the catalytic electrode have also received considerable attention recently (<xref ref-type="bibr" rid="B114">Logan and Regan, 2006</xref>; <xref ref-type="bibr" rid="B199">Tarpeh et al., 2018</xref>). The latter is predominantly operative for highly saline wastewaters, especially for brine and tannery wastewaters. Biological techniques such as bioelectrochemical systems, enzymatic catalysis, and microalgae cultivation have been employed to remediate wastewater of a wide range along with the generation of various value-added compounds (<xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>; <xref ref-type="bibr" rid="B227">Yadav et al., 2022</xref>). In contrast, biological approaches are more technologically sound than Physico-chemical approaches available for wastewater treatment and valorisation due to their sturdiness, goal-specific, eco-friendly and resilient characteristics. However, the capital and operational costs used for wastewater treatment and valorisation are important to consider while deciding which method to use, as they can have a big impact on the overall cost of the project.</p>
<p>Therefore, the present article highlights the most novel approaches for wastewater valorisation and the generation of value-added products (such as biofuels, biofertilisers, and biopesticides) and recovery of biopolymers, vitamins, enzymes, dyes, pigments, and phenolic compounds. In addition, we have addressed the life cycle assessment and a critical overview of the barriers to the large-scale application of resource recovery strategies and economic, environmental, and social concerns associated with using waste-derived products.</p>
</sec>
<sec id="s2">
<title>2 Novel approaches for wastewater treatment</title>
<sec id="s2-1">
<title>2.1 Membrane technology</title>
<p>Membrane separation is one of the cutting-edge technologies for wastewater treatment. Here, a permeable membrane is used to let wastewater pass through it. Any solute larger than the membrane&#x2019;s pore size will be restricted, while the remaining solution passes through the membrane. The nutrients/solutes trapped in the filter cake are continuously removed throughout this filtration process to ensure the consistence of filtration process. Based on the size of the pores present in the membranes, we may categorise the membrane separation processes (<xref ref-type="bibr" rid="B119">Mahmoud et al., 2022a</xref>) into four categories, (i) RO/FO (Reverse osmosis/Forward osmosis), (ii) NF (Nanofiltration), (iii) UF (Ultrafiltration), and (iv) MF (Microfiltration) (<xref ref-type="fig" rid="F2">Figure 2</xref>).</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Pressure driven membrane systems with their characteristic properties.</p>
</caption>
<graphic xlink:href="fceng-05-1129783-g002.tif"/>
</fig>
<p>Pore size, structure, and operational pressure are the fundamental properties of pressure-driven membranes. MF uses a precise sieving mechanism along with cutting-edge, environmentally friendly technology. It has extensive industrial applications in food and dairy industry, textile industry, biotechnology, and pharmaceutical industry (<xref ref-type="bibr" rid="B64">Foorginezhad and Zerafat, 2017</xref>; <xref ref-type="bibr" rid="B90">Khan and Boddu, 2021</xref>). The feasibility of MF was reported by <xref ref-type="bibr" rid="B128">Marchesi et al. (2019)</xref> for the recycling and reuse of chicken pre-chiller wastewater owing to its high rejection efficiency (up to 92.5% of COD, 89.1% of TOC, and 100% of microbes). However, UF membranes work on the principle of size exclusion, which have pores with a size range of 0.005&#x2013;0.1&#xa0;&#x3bc;m. However, additional elements, including molecular structure, charge, and hydrodynamic circumstances, can also significantly impact the rejection efficiency (<xref ref-type="bibr" rid="B4">al Aani et al., 2020</xref>). The use of UF for separating proteins from food industry wastewater has been reported frequently. NF membranes&#x2019; pore sizes range from 0.1 to 10&#xa0;mm. It can display intense permeate flux and significant macromolecule rejection. While NF has been used to recover comparatively smaller molecules such as lactose and phenols (<xref ref-type="bibr" rid="B103">Lee and Stuckey, 2022</xref>). According to <xref ref-type="bibr" rid="B156">Pronk et al. (2006)</xref>, the NF membrane have potential to discard micropollutants such as phosphate, diclofenac, propanol, carbamazepine, and ibuprofen while allowing nitrogen to pass through for its recovery.</p>
<p>NF and RO are high-pressure membrane processes, therefore, frequently employed to recover ammonium from greywater as they significantly reject the salts and ions (<xref ref-type="bibr" rid="B1">Adam et al., 2018</xref>; <xref ref-type="bibr" rid="B163">Ray et al., 2020</xref>). In the RO process, feed water is propelled through a semipermeable membrane from a dilute to a concentrated solution by the difference in osmotic pressure (<xref ref-type="bibr" rid="B3">Ahuchaogu et al., 2018</xref>). <xref ref-type="bibr" rid="B163">Ray et al. (2020)</xref>, reported successful recovery (64%&#x2013;90%) of unionised ammonia from hydrolysed urine by using RO and NF procedures. However, the high expense of the process of nutrient recovery from wastewater is a drawback for NF and RO (<xref ref-type="bibr" rid="B223">Xu et al., 2017</xref>). Other factors can further increase operational costs, including membrane fouling, a decrease in membrane shelf life, and reduced rejection efficiency (<xref ref-type="bibr" rid="B180">Shi et al., 2014</xref>). As a result, effective treatment and valorisation methods are needed for treatment and resource recovery, such as FO technology, which is highly operative in the case of specific target molecules.</p>
<p>In order to recover nutrients from the wastewater and produce clean water, the nitrogen and phosphorous in primary treated municipal wastewater can be concentrated by the FO membrane method (<xref ref-type="bibr" rid="B83">Jafarinejad, 2021</xref>). Due to the size-sieving action of FO membranes, high rejection efficiency for the majority of nutrients, including the high-in-demand phosphate, has been well documented in the literature (<xref ref-type="bibr" rid="B112">Linares et al., 2013</xref>; <xref ref-type="bibr" rid="B113">Liu et al., 2019</xref>). If the technological and operational shortcomings can be successfully resolved, membrane technology is anticipated to attract more interest and profitability in this market segment in the upcoming years (<xref ref-type="table" rid="T1">Table 1</xref>).</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Different membrane technologies with their removal efficiency.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Wastewater type</th>
<th align="left">Membrane</th>
<th align="left">Material</th>
<th align="left">Removal efficiency</th>
<th align="left">References</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left"/>
<td align="left">MF</td>
<td align="left">Polyether sulfone</td>
<td align="left">92.5% COD, 82.5% TN</td>
<td align="left">
<xref ref-type="bibr" rid="B128">Marchesi et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="left">Textile wastewater</td>
<td align="left">FO</td>
<td align="left">Aquaporin based</td>
<td align="left">&#x3e;94% COD, &#x3e;99% TDS, TSS, Zn<sup>2&#x2b;</sup>, and SO<sub>4</sub>, 55% water recovery</td>
<td align="left">
<xref ref-type="bibr" rid="B95">Korenak et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="left">Acidic wastewater</td>
<td align="left">NF</td>
<td align="left"/>
<td align="left">94% heavy metal ions</td>
<td align="left">
<xref ref-type="bibr" rid="B230">You et al. (2017)</xref>
</td>
</tr>
<tr>
<td align="left">Digested swine wastewater</td>
<td align="left">FO</td>
<td align="left"/>
<td align="left">&#x3e;93% ammonium nitrogen, &#x3e;50% water recovery</td>
<td align="left">
<xref ref-type="bibr" rid="B221">Wu et al. (2018)</xref>
</td>
</tr>
<tr>
<td align="left">Molasses distillery wastewater</td>
<td align="left"/>
<td align="left"/>
<td align="left">85.2% COD, 97.3% melanoidins, 65% water recovery</td>
<td align="left">
<xref ref-type="bibr" rid="B184">Singh et al. (2018)</xref>
</td>
</tr>
<tr>
<td align="left">Activated sludge from wastewater treatment Plants (WWTP)</td>
<td align="left">FO</td>
<td align="left">Flat-sheet CTA</td>
<td align="left">96% ammonium nitrate, 98% phosphate, 99% OC</td>
<td align="left">
<xref ref-type="bibr" rid="B145">Nguyen et al. (2013)</xref>
</td>
</tr>
<tr>
<td align="left">Municipal primary effluent</td>
<td align="left">FO-RO</td>
<td align="left"/>
<td align="left">100% ammonia, fluoride, and phosphate, 90% CaSO<sub>4</sub> and OC, 86%&#x2013;89% K and Mg</td>
<td align="left">
<xref ref-type="bibr" rid="B85">Jiang et al. (2020)</xref>
</td>
</tr>
<tr>
<td align="left">Treated sewage effluent</td>
<td align="left">FO</td>
<td align="left">Flat sheet TFC</td>
<td align="left">99%, total phosphorus, 97% ammonium</td>
<td align="left">
<xref ref-type="bibr" rid="B72">Hafiz et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="left">Textile wastewater</td>
<td align="left">MF</td>
<td align="left">PEG, Clay and Zeolite composite</td>
<td align="left">5.55% crystal violet, 90.23% methylene blue</td>
<td align="left">
<xref ref-type="bibr" rid="B64">Foorginezhad, and Zerafat (2017)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s2-2">
<title>2.2 Enzymatic catalysis</title>
<p>Enzymes, which are fundamental to all biological activities, are highly effective biocatalysts that speed up chemical reactions under physiological conditions by breaking down complex compounds into simpler ones (<xref ref-type="bibr" rid="B16">Bell et al., 2021</xref>). Many wastewaters contain heavy grease content, dyes, lignocellulosic mass, agrochemicals, blood, tissues, pathogens, and other emerging contaminants from food processing industries, restaurants, dairy, oil refineries, meat processing, tannery, slaughterhouse, cosmetics, and pharmaceuticals industries (<xref ref-type="bibr" rid="B121">Mahmoud et al., 2016</xref>; <xref ref-type="bibr" rid="B125">Mahmoud et al., 2018</xref>; <xref ref-type="bibr" rid="B118">Mahmoud et al., 2021b</xref>; <xref ref-type="bibr" rid="B91">Khan et al., 2022</xref>; <xref ref-type="bibr" rid="B117">Mahmoud, 2022</xref>). If left untreated, such wastewater can cause severe environmental pollution, potentially contributing to the spread of these pollutants into the various environmental matrices and eventually threatening human health (<xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>).</p>
<p>Treatment and valorisation methods based on enzymatic catalysis offer numerous advantages over conventional methods, such as low energy input, low toxicity, the ability to function under mild conditions, abridged sludge, and byproduct generation (<xref ref-type="bibr" rid="B171">Rout et al., 2022</xref>) (<xref ref-type="table" rid="T2">Table 2</xref>). Enzymes can be used in both free form and immobilised forms however, the enzymes&#x2019; storage stability and operation ability upsurge upon immobilisation. The development in enzyme reutilisation and recoverability, that elevates its productivity and lowers the entire process&#x2019;s cost, is the most crucial benefit of the immobilised enzyme (<xref ref-type="bibr" rid="B36">Chen et al., 2019</xref>; <xref ref-type="bibr" rid="B101">Lassouane et al., 2019</xref>). Predominantly, enzymes <italic>viz.</italic> laccases, tyrosinases, lipases, cellulases, lignin, and phenol peroxidases hold a promising role in mitigating any kind of contamination from an extensive array of wastewater types such as greasy wastewater, sugarcane industry wastewaters, dairy wastewaters, pharmaceutical industry, tannery textile, paper and pulp, mining, etc. in a precise, manageable, and controlled manner (<xref ref-type="bibr" rid="B26">Brugnari et al., 2018</xref>; <xref ref-type="bibr" rid="B36">Chen et al., 2019</xref>).</p>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Enzymes used in wastewater treatment with removal efficiencies.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Enzymes</th>
<th align="left">Form of enzyme</th>
<th align="left">Pollutants</th>
<th align="left">Wastewater</th>
<th align="left">Removal efficiency</th>
<th align="left">References</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Laccase</td>
<td align="left">Immobilized</td>
<td align="left">Phenolic compounds</td>
<td align="left"/>
<td align="left">80%</td>
<td align="left">
<xref ref-type="bibr" rid="B225">Yadav et al. (2021)</xref>
</td>
</tr>
<tr>
<td align="left">Laccase</td>
<td align="left">Free form</td>
<td align="left">Dyes</td>
<td align="left">textile wastewater</td>
<td align="left">50%</td>
<td align="left">
<xref ref-type="bibr" rid="B140">Motamedi et al. (2021)</xref>
</td>
</tr>
<tr>
<td align="left">Lipase</td>
<td align="left">Immobilised</td>
<td align="left">Melanoidins</td>
<td align="left">Sugar mill wastewater</td>
<td align="left">84%&#x2013;86%</td>
<td align="left">
<xref ref-type="bibr" rid="B220">Wei et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="left">Lacasse</td>
<td align="left">Immobilised</td>
<td align="left"/>
<td align="left">Meat industry wastewater</td>
<td align="left"/>
<td align="left">
<xref ref-type="bibr" rid="B201">Thirugnanasambandham and Sivakumar (2015)</xref>
</td>
</tr>
<tr>
<td align="left">Horseradish peroxidase</td>
<td align="left">Immobilised</td>
<td align="left">Reactive Black dye and Malachite green</td>
<td align="left"/>
<td align="left">70%</td>
<td align="left">
<xref ref-type="bibr" rid="B84">Jankowska et al. (2021)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Lipase is a class of hydrolase enzymes with multiple benefits and high catalytic rates (<xref ref-type="bibr" rid="B146">Nimkande and Bafana, 2022</xref>). lipases have both high catalytic efficiency and substrate specificity, enabling it to achieve excellent wastewater treatment efficiencies (<xref ref-type="bibr" rid="B10">Ariaeenejad et al., 2023</xref>). For instance, lipase consortium from <italic>Pseudomonas aeruginosa</italic> was utilised for the remediation of restaurant wastewater by <xref ref-type="bibr" rid="B196">Sutar et al. (2023)</xref>. Another class of enzyme, laccase, was found to be effective in degradation of phenolic compounds such as the very unfamous Bisphenol A, an endocrine disruptor, commonly used in plastic production, and barely degraded in conventional wastewater treatment systems. The laccase from <italic>Pleurotus ostreatus</italic> immobilised onto mono aminoethyl-N-aminoethyl agarose achieved 90% removal efficiency of BPA in 15 catalytic cycles (<xref ref-type="bibr" rid="B26">Brugnari et al., 2018</xref>). Additionally, <xref ref-type="bibr" rid="B101">Lassouane et al. (2019)</xref> employed immobilised laccase from <italic>Trametes pubescens</italic> to remove BPA. at pH 5 and temperature at 30&#xb0;C, this biocatalytic system aided the degradation of BPA with 100% contaminant removal efficiency within 2&#xa0;hours. In a different study, <xref ref-type="bibr" rid="B36">Chen et al. (2019)</xref> degraded nine pesticides, owing to immobilised laccase enzyme, using wheat straw and peanut shells as supports for the reaction system, and syringaldehyde to enhance the catalytic characteristics of the laccase. 54.5% decomposition rate was achieved using laccase immobilised on peanut shells. However, the reaction efficiency rose to 65.9% when wheat straw was utilised.</p>
<p>Although enzyme technology in wastewater treatment has a promising role, it has its limitations that need to be addressed. An efficient immobilisation system can circumvent these challenges by enhancing enzyme stability, thereby increasing the shelf life of the enzymes in the reaction system.</p>
</sec>
<sec id="s2-3">
<title>2.3 Microalgae cultivation</title>
<p>Urban, agricultural, and industrial activities produce massive amounts of nutrients rich wastewater, which would inevitably result in eutrophication in the aquatic environment as well as the threat of releasing harmful emerging contaminants that can enter the food chain and pose a risk to human health (<xref ref-type="bibr" rid="B80">Iqbal et al., 2022</xref>; <xref ref-type="bibr" rid="B135">Minhas et al., 2022</xref>).</p>
<p>Central and local governments should follow strict laws and regulations to limit the pollutants released into the environment. They should also work to reclaim and reuse resources, such as water, in order to improve the current state of the environment and promote the use of a circular economy that focuses on reducing waste and reusing resources (<xref ref-type="bibr" rid="B19">Bolger and Doyon, 2019</xref>; <xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>). However, the majority of currently used methods for treating sewage and wastewater, such as the aerobic activated sludge-based treatment process, nitrification-denitrification, chemical phosphorus removal, and coagulating sedimentation, face difficulties due to their high energy requirements, unstable treatment effects, lengthy processes, carbon emissions, excess sludge discharge, and waste of recyclable resources (<xref ref-type="bibr" rid="B175">Sathya et al., 2022</xref>). These challenges are also clear impediments to integrating wastewater treatment with low-carbon emissions, low-energy consumption, and resource recycling (<xref ref-type="bibr" rid="B71">Gu et al., 2017</xref>).</p>
<p>One of the most forefront technologies for wastewater treatment is the microalgae-based treatment process for advanced treatment, valorisation and nutrient recovery (<xref ref-type="fig" rid="F3">Figure 3</xref>). Microalgae includes photosynthetic microorganisms that can thrive easily in industrial and municipal wastewaters, remediate it and produce biomass rich in nutrients, bioactive compounds, biomolecules, and other value-added products (<xref ref-type="bibr" rid="B48">Daneshvar et al., 2018</xref>; <xref ref-type="bibr" rid="B136">Mishra et al., 2022</xref>). Moreover, these form the raw materials for generating value-added products, energy, and economy along with the bioremediation process simultaneously (<xref ref-type="bibr" rid="B134">Michelon et al., 2021</xref>). Microalgae&#x2019;s strong nutrient removal efficiency in the advanced treatment of urban, agricultural, and industrial wastewater have made it possible to use it as a supplement for tertiary wastewater treatment (<xref ref-type="bibr" rid="B171">Rout et al., 2022</xref>). Cultivation of microalgae from wastewater utilises the nutrients present in the wastewater to support its growth and allows the reduction of production costs and greenhouse gas emissions (<xref ref-type="bibr" rid="B136">Mishra et al., 2022</xref>; <xref ref-type="bibr" rid="B50">Dias et al., 2023</xref>). To date, a wide range of microalgae species (Scenedesmus, Botryococcus, Chlorella, Dunaliella, Parachlorella, etc.) have been reported to be used in valorisation and treatment of wide range of wastewaters (<xref ref-type="bibr" rid="B7">Amini et al., 2020</xref>) as mentioned in <xref ref-type="table" rid="T3">Table 3</xref>.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>Wastewater valorisation and production of value-added products using microalgae cultivation.</p>
</caption>
<graphic xlink:href="fceng-05-1129783-g003.tif"/>
</fig>
<table-wrap id="T3" position="float">
<label>TABLE 3</label>
<caption>
<p>Microalgae cultivation in wastewater treatment with nutrients recovery.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Algae</th>
<th align="left">Wastewater</th>
<th align="left">COD removal rate (%)</th>
<th align="left">Ammonium removal rate (%)</th>
<th align="left">Total N removal rate (%)</th>
<th align="left">Total <italic>p</italic> removal rate (%)</th>
<th align="left">References</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">
<italic>Chlorella vulgaris</italic>
</td>
<td align="left">Municipal wastewater</td>
<td align="left">75</td>
<td align="left"/>
<td align="left">70</td>
<td align="left">53</td>
<td align="left">
<xref ref-type="bibr" rid="B7">Amini et al. (2020)</xref>
</td>
</tr>
<tr>
<td align="left">Microalgae consortium</td>
<td align="left">Tannery wastewater</td>
<td align="left">56.7</td>
<td align="left"/>
<td align="left">71.7</td>
<td align="left">97.6</td>
<td align="left">
<xref ref-type="bibr" rid="B154">Pena et al. (2020)</xref>
</td>
</tr>
<tr>
<td align="left">
<italic>Scendesmus</italic>
</td>
<td align="left">Molasses wastewater</td>
<td align="left">87.2</td>
<td align="left"/>
<td align="left">90.5</td>
<td align="left">88.6</td>
<td align="left">
<xref ref-type="bibr" rid="B116">Ma et al. (2017)</xref>
</td>
</tr>
<tr>
<td align="left">
<italic>Ascochloris</italic>sps ADW007</td>
<td align="left">Dairy wastewater</td>
<td align="left">94&#x2013;96</td>
<td align="left"/>
<td align="left">72&#x2013;80</td>
<td align="left">80&#x2013;97</td>
<td align="left">
<xref ref-type="bibr" rid="B96">Kumar et al. (2019)</xref>
</td>
</tr>
<tr>
<td align="left">
<italic>Chlorella vulgaris</italic>
</td>
<td align="left">Livestock farm wastewater</td>
<td align="left">62.3</td>
<td align="left">81.2</td>
<td align="left"/>
<td align="left">85.3</td>
<td align="left">
<xref ref-type="bibr" rid="B115">Lv et al. (2018)</xref>
</td>
</tr>
<tr>
<td align="left">
<italic>Chlorella vulgaris</italic>
</td>
<td align="left">Piggery and brewery wastewater</td>
<td align="left">93</td>
<td align="left">100</td>
<td align="left">96</td>
<td align="left">90</td>
<td align="left">
<xref ref-type="bibr" rid="B235">Zheng et al. (2018)</xref>
</td>
</tr>
<tr>
<td align="left">
<italic>Chlorella sorokiniana</italic>
</td>
<td align="left">Dairy wastewater</td>
<td align="left">86.8</td>
<td align="left"/>
<td align="left">80.7</td>
<td align="left">94.6</td>
<td align="left">
<xref ref-type="bibr" rid="B100">Kusmayadi et al. (2022)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Microalgae can tolerate a wide range of water salinity, pH, and temperature. They can also grow in high concentrations of oxides of sulfur, carbon and nitrogen, making them suitable for wastewater cultivation (<xref ref-type="bibr" rid="B54">Ebhodaghe et al., 2022</xref>). <italic>Scenedesmus quadricauda</italic> and <italic>Tetraselmis suecica</italic>, two freshwater and marine water strains, have recently been studied by <xref ref-type="bibr" rid="B48">Daneshvar et al. (2018)</xref> for the treatment of dairy wastewater. While <italic>T. suecica</italic> strain removed 86.21% of TN, 44.92% of <italic>p</italic>, and 40.16% of total organic carbon, this strain had an efficiency of removal of 86.21% TN, 64.47% phosphate, and 42.18% TOC. Additionally, 295.34 and 56.25&#xa0;mg g-1 of tetracycline could be removed from water by each species, respectively (<xref ref-type="bibr" rid="B48">Daneshvar et al., 2018</xref>).</p>
</sec>
</sec>
<sec id="s3">
<title>3 Resource recovery from wastewater and sludge</title>
<p>Wastewater may be beheld as a reservoir of resources as it contains a wide array of nutrients and components that can be valorised into value-added products such as fertilisers, biofuels, biopesticides and many more (<xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>). Wastewater sources, including wastewater and sludge, are rich in nutrients and are now recognised as important sources of nutrients. Nutrient recovery such as phosphorus and nitrogen, from wastewater can make wastewater treatment more sustainable, also reduce the costs associated with removing these nutrients from the wastewater, and provide additional fertilisers that can be used to help grow food (<xref ref-type="bibr" rid="B237">Zin and Kim, 2021</xref>; <xref ref-type="bibr" rid="B77">Hui et al., 2022</xref>). For the treatment of wastewater and concurrent resource recovery and production of value-added products (nutrients, organic acids, bioplastics, bio-pesticides, bio-surfactants, bio-flocculants etc.) as well as bioenergy, biofuels, and bioelectricity, more advanced and novel technologies are currently being identified and fundamentally considered. Numerous technologies, including conventional ones like chemical precipitation and adsorption and more cutting-edge ones like bio electrochemical systems and osmotic membrane bioreactors, have been successfully examined for their efficacy in nutrient recovery (<xref ref-type="bibr" rid="B99">Kurup et al., 2019</xref>; <xref ref-type="bibr" rid="B143">Nazir et al., 2019</xref>; <xref ref-type="bibr" rid="B29">Canadas et al., 2022</xref>).</p>
<sec id="s3-1">
<title>3.1 Recovery of nutrients (phosphate, nitrates, ammonia, proteins, lipids, vitamins)</title>
<p>A crucial step toward sustainable development is the recovery of nutrients from wastewaters and sludge. Urban and industrial wastewater are potential raw materials to recover significant biologically active components. Sewage sludge from wastewater treatment facilities provide rich source of biomolecules that include, nutrients such as NPK, antioxidants, lipids, proteins, enzymes, carbohydrates, vitamins, nitrogen, phosphates, minerals, ammonium compounds, and many more (<xref ref-type="bibr" rid="B236">Zhu et al., 2017</xref>; <xref ref-type="bibr" rid="B35">Chen et al., 2020</xref>; <xref ref-type="bibr" rid="B182">Sichler et al., 2022</xref>).</p>
<p>Due to the commercialization of agriculture and the need to feed an expanding population, the demand for fertiliser has increased over the past few decades. By 2022, it has already been predicted that most regions of the world will experience a shortage of at least one NPK fertiliser, Moreover, In 2014, the European Commission added phosphate rock to the list of critical raw materials for the first time (<xref ref-type="bibr" rid="B55">EC, 2014</xref>). Scientists are looking at alternatives to provide these crucial agricultural nutrients due to the restricted availability and the high cost of production. Compared to nitrogen and phosphorus, potassium has not yet had a significant economic impact on agriculture because, at the pace it is being consumed, there are more than 330&#xa0;years of reserves. In contrast, there is no substitute for phosphorus in agricultural output and its supply is expected to run out in 100&#xa0;years, making it a limited resource and a critical commodity (<xref ref-type="bibr" rid="B43">Cordell et al., 2009</xref>).</p>
<p>Municipal wastewater and sludge, offer a promising secondary phosphorus source, comprising around 40% of the phosphorus in human excreta (<xref ref-type="bibr" rid="B44">Cordell and White, 2014</xref>; <xref ref-type="bibr" rid="B94">Klinglmair et al., 2015</xref>). Several techniques, such as biological release, pH adjustment, ozonation, mechanical treatment, and heat treatment, have been used to recover phosphorus from municipal wastewater and sewage sludge (<xref ref-type="bibr" rid="B224">Xue and Huang, 2007</xref>; <xref ref-type="bibr" rid="B161">Quist-Jensen et al., 2018</xref>; <xref ref-type="bibr" rid="B219">Wang et al., 2021</xref>). Notably, the total amount of phosphorus found in human waste (urine and excreta) may meet around 22% of the world&#x2019;s phosphorus needs (<xref ref-type="bibr" rid="B44">Cordell and White, 2014</xref>). However, due to worries about possible infections, persistent organic pollutants, heavy metals, and odor, direct wastewater and sludge application to agriculture is regarded as unsafe in many places (<xref ref-type="bibr" rid="B39">Cieslik et al., 2015</xref>). Therefore, nutrient recovery is considered the best way to confiscate phosphorous, nitrogen, ammonium, and other nutrients to support sustainability by putting less stress on natural gas and other renewable energy sources spent on producing these nutrients (<xref ref-type="bibr" rid="B200">Theregowda et al., 2019</xref>; <xref ref-type="bibr" rid="B59">Ersahin et al., 2023</xref>).</p>
<p>Agents like magnesium, calcium, and other alkaline metals are introduced in the precipitation process to change pH and create the precipitate (<xref ref-type="bibr" rid="B149">Owodunni et al., 2023</xref>). Nutrient recovery from sludge centrates is largely accomplished commercially through chemical precipitation and crystallization (<xref ref-type="bibr" rid="B133">Melia et al., 2017</xref>). Sludge centrate is low in volume but high in phosphate and ammonium concentration when compared to wastewater discharge. The dry mass of wastewater sludge can contain up to 15% phosphorus, which is typically coupled to metal ions like calcium, iron, and aluminium or contained in biomass (<xref ref-type="bibr" rid="B231">Yu et al., 2021</xref>). The possibility of recovering phosphorus from wastewater sludge will be greatly increased by leaching phosphorus into the aqueous phase. Due to the dissolution of inorganic phosphorus, acidification is one of the most successful methods (<xref ref-type="bibr" rid="B160">Quist-Jensen et al., 2020</xref>).</p>
<p>In a study, phosphate and ammonium nitrate were recovered from sewage sludge ash and food industry wastewater using Mg-Biochar derived from ground coffee bean and palm tree trunk waste. Palm tree trunk Mg-biochar could recover 92.2% of phosphate and 54.8% of ammonium nitrate, while ground coffee bean biochar recovered 79.5% of phosphate and 38.6% ammonium (<xref ref-type="bibr" rid="B237">Zin and Kim, 2021</xref>). Besides, wastewaters also are a rich source of nutrients such as proteins, lipids, vitamins, etc. Several industries generate copious volumes of protein-laden wastewater. Starch processing water from the potato manufacturing industry is known to have a high content of protein, where foam separation and membrane technology by ultrafiltration are used for its recovery (<xref ref-type="bibr" rid="B46">Dabestani et al., 2017</xref>).</p>
<p>Similarly, multiple industrial, domestic wastewater, and sewage sludge are rich source of proteins. Bulk proteins have countless industrial applications, in manufacturing of food and beverages, personal care products, medicines, cosmetics and animal feed. The most common use of bulk proteins derived from waste is in animal feed (<xref ref-type="bibr" rid="B167">Ritala et al., 2017</xref>). <xref ref-type="bibr" rid="B78">Hwang et al. (2008)</xref> recovered protein from sludge to be used as animal feed by the method of sludge disintegration. Precipitation and drying methods were used to separate the soluble proteins from the sludge. This concept is feasible because sludge typically contains beneficial organic substances such as nucleic acids, enzymes, proteins, and polysaccharides (<xref ref-type="bibr" rid="B87">Jung et al., 2002</xref>). Protein has been estimated to account for approximately half of the dry weight of bacterial cells (<xref ref-type="bibr" rid="B181">Shier and Purwono, 1994</xref>). Protein is one of the most vital elements in animal feed, providing energy and nitrogen (<xref ref-type="bibr" rid="B2">Adebayo et al., 2004</xref>). Single-cell protein (SCP) is a type of protein that is made from microbial biomass and is commonly used as an additive in animal feed. It is less expensive to produce SCP using microbial communities, which are groups of different types of microorganisms, than it is to produce it using a single type of organism (<xref ref-type="bibr" rid="B214">Vethathirri et al., 2021</xref>). Furthermore, protein recovery also facilitates wastewater discharge by significantly reducing the Biological Oxygen Demand (BOD) and COD (<xref ref-type="bibr" rid="B27">Buchanan et al., 2023</xref>). Like proteins, Lipids have a variety of industrial applications in a variety of products, including manufacturing and production of biodiesel, agrochemicals, animal feed, personal care items, and cosmetics (<xref ref-type="bibr" rid="B49">De Luca et al., 2021</xref>) to name a few.</p>
<p>Physical methods of extracting and recovering proteins and lipids from wastewater and sewage sludge involve using adsorption, microwaves, ultrasonics, heat, centrifuges, and membrane filtration. Chemical processes involve using thermal alkali, thermal acidic, pH regulation, and ethylenediamine tetraacetic acid (EDTA). <xref ref-type="bibr" rid="B77">Hui et al. (2022)</xref>, conducted a study to isolate proteins from waste-activated sludge (WAS). Maximum protein concentration (549.86&#xa0;mg/L) was recovered with high extraction rate (60.72%) under alkaline conditions at 70&#xb0;C. The relative molecular weight of the sludge proteins was between 6.5&#xa0;kDa and 16&#xa0;kDa. <xref ref-type="bibr" rid="B99">Kurup et al. (2019)</xref> demonstrated the use of low-cost Na-lignosulphonate to recover lipids and proteins from dairy industry effluents. He reported that change in Na-lignosulphonate concentration (0.002%&#x2013;0.032%, w/v), medium&#x2019;s pH (1.0&#x2013;3.5) and the temperature (22&#xb0;C and 40&#xb0;C) enhanced the rate of precipitation in the wastewater samples. The procedure was highly effective (96% of lipids and proteins recovery and 73% BOD removal at 22&#xb0;C) over methanol and chloroform-based solvent extraction of lipids which is neither cost-effective nor environmentally beneficial. In another study on the extraction of lipids from synthetic primary sludge by <xref ref-type="bibr" rid="B215">Villalobos-Delgados et al. (2021)</xref>, the lipid component was successfully recovered using ethyl butyrate (13%&#x2013;23% of the total solids).</p>
</sec>
<sec id="s3-2">
<title>3.2 Recovery of phenolic compounds</title>
<p>Phenol is a significant environmental contaminant that may result in water pollution. Natural occurrences or anthropogenic activities are the two critical sources. In nature phenol is produced when dead plants and animals decompose in water. Humans utilise phenol in their daily activities in chemical production or petrochemical industries. Alkylphenols, cresols, and resin are also synthesized using it as a precursor (<xref ref-type="bibr" rid="B30">Careghini et al., 2015</xref>). The building business in the wood sector mainly provided phenolic resin and appliances to suit varied needs (<xref ref-type="bibr" rid="B197">Takeichi and Furukawa, 2012</xref>). Additionally, phenol is a key component of explosives, textile industries, and dyes (<xref ref-type="bibr" rid="B189">Stamatelatou et al., 2011</xref>; <xref ref-type="bibr" rid="B153">Patel and Vashi, 2015</xref>). Epoxy resins and polycarbonate plastics are commonly made using phenolic replacements like bisphenol A (<xref ref-type="bibr" rid="B187">Sirasanagandla et al., 2022</xref>).</p>
<p>Some industries including the food industry, paper and pulp manufacturing, and wood distillation produce phenol, specifically chloro-phenol, as part of their processes (<xref ref-type="bibr" rid="B148">Olaniran and Igbinosa, 2011</xref>). These industrial activities directly or indirectly release phenol-containing wastewater into water bodies, resulting in water contamination. Phenol contamination of the water sources would result from the runoff of the agrochemicals such as pesticides and herbicides (<xref ref-type="bibr" rid="B11">Badanthadka and Mehendale, 2014</xref>). Domestic and municipal sources of phenol discharge into water sources were also a factor in addition to the industrial sector (<xref ref-type="bibr" rid="B217">Villegas et al., 2016</xref>; <xref ref-type="bibr" rid="B142">Mu&#x2019;azu et al., 2017</xref>).</p>
<p>Olive Mill Wastewaters (OMWW) are a great source of phenolic chemicals. These phenolic substances pose a serious threat to aquatic life, microbes, and plants since they are both extremely phytotoxic and resistant (<xref ref-type="bibr" rid="B34">Chedeville et al., 2009</xref>; <xref ref-type="bibr" rid="B88">Kathi, 2022</xref>). Wastewater toxicity may suppress the microbial population, therefore, biological treatment facilities are insufficient. Hence, it is essential that phenolic wastewater be properly treated before its discharge (<xref ref-type="bibr" rid="B194">Sun et al., 2015</xref>). Despite the fact that these techniques have already been created and proposed, they have not produced satisfying outcomes (<xref ref-type="bibr" rid="B147">Ochando-Pulido et al., 2013</xref>). An integrated approach is necessary for the practical management of OMWW.</p>
<p>The combination of membrane processes, such as MF, UF, NF, and RO, is recommended as a good alternative in this regard by a number of studies (<xref ref-type="bibr" rid="B233">Zagklis et al., 2015</xref>; <xref ref-type="bibr" rid="B15">Bazzarelli et al., 2016</xref>; <xref ref-type="bibr" rid="B143">Nazir et al., 2019</xref>) (<xref ref-type="table" rid="T4">Table 4</xref>). Solvent extraction is popularly used on OMWW to recover phenolic compounds (<xref ref-type="bibr" rid="B70">Goula and Gerasopoulos, 2017</xref>). In order to get all of the phenolic compounds out of the OMWW, different solvents are needed that make the process more complicated, take longer time, and cost more currency (<xref ref-type="bibr" rid="B206">Tsakona et al., 2012</xref>; <xref ref-type="bibr" rid="B65">Galanakis. 2013</xref>). Adsorption is considered the most appropriate method for recovering OMWW phenolic compounds because it is cost-efficient and commonly used (<xref ref-type="bibr" rid="B123">Mahmoud et al., 2020</xref>; <xref ref-type="bibr" rid="B122">Mahmoud et al., 2022b</xref>).</p>
<table-wrap id="T4" position="float">
<label>TABLE 4</label>
<caption>
<p>Phenolic compounds recovery methods from different wastewaters.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Wastewater type</th>
<th align="left">Method used</th>
<th align="left">Recovered phenols</th>
<th align="left">Recovery percentage</th>
<th align="left">References</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Winery wastewater</td>
<td align="left">Biobased liquid-liquid extraction method</td>
<td align="left">Gallic acid, protocatechuic acid, 4-hydroxybenzoic acid, caffeic acid, vanillic acid, syringic acid</td>
<td align="left">96.46%, 87.44%, 80.82% 92.24% 75.18% 38.19%</td>
<td align="left">
<xref ref-type="bibr" rid="B29">Canadas et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="left">Phenolic wastewater</td>
<td align="left">Magnetic ionic liquid aqueous two-phase separation along with thermoseparation</td>
<td align="left">Phenol, o-cresol, m-cresol</td>
<td align="left">94.18%, 98.35%, 97.81%</td>
<td align="left">
<xref ref-type="bibr" rid="B228">Yao et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="left">Municipal Wastewater sludge</td>
<td align="left">Biochar assisted hydrothermal liquefaction sorption</td>
<td align="left">5-Hydroxyindoleacetate, 4-Hydroxyphenylacetate, 4-Hydroxybenzoate, sodium salicylate, scytalone, maculosin, biphenyl-2,3-diol, biphenyl-2,3-diol, candicine, chrysosplenetin, abyssinone V, and hydroxyanthraquinone</td>
<td align="left">66%&#x2013;99%</td>
<td align="left">
<xref ref-type="bibr" rid="B218">Wang et al. (2022)</xref>
</td>
</tr>
<tr>
<td align="left">Olive mill wastewateter</td>
<td align="left">Pomegranate peel and orange waste-based adsorbent</td>
<td align="left"/>
<td align="left">93.13%, 89.5%</td>
<td align="left">
<xref ref-type="bibr" rid="B213">Ververi and Goula (2019)</xref>
</td>
</tr>
<tr>
<td align="left">Winery sludge</td>
<td align="left">Ultrafiltration</td>
<td align="left">Hydroxycinnamic acids, o-diphenols</td>
<td align="left">81%</td>
<td align="left">
<xref ref-type="bibr" rid="B65">Galanakis (2013)</xref>
</td>
</tr>
<tr>
<td align="left">Artichoke wastewaters</td>
<td align="left">Nanofiltration</td>
<td align="left">Chlorogenic acid, Apigenin-7-O-glucoside</td>
<td align="left">100%</td>
<td align="left">
<xref ref-type="bibr" rid="B42">Conidi et al. (2015)</xref>
</td>
</tr>
<tr>
<td align="left">Orange press liquor</td>
<td align="left">Nanofiltration</td>
<td align="left">Anthocyanins (cyanidin-3-glucoside chloride, myrtillin chloride and peonidin-3-glucoside chloride), flavanone</td>
<td align="left">&#x3e;65%</td>
<td align="left">
<xref ref-type="bibr" rid="B31">Cassano et al. (2014)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s3-3">
<title>3.3 Recovery of dyes and pigments</title>
<p>In the production of pharmaceuticals, textiles, food, paper and pulp, and cosmetics, synthetic dyes are utilised. Water is used extensively throughout the fixing, dying, and washing stages of the textile industry&#x2019;s dyeing process. The dyes are organic soluble substances that can be categorised as direct, reactive, acidic, or basic. Due to their great solubility in water, dyes are more difficult to remove using standard methods. The main carcinogenic and hazardous pollutants are industrial dyes and their byproducts.</p>
<p>A number of studies demonstrate the harmful effects of azo dyes on plant growth and germination. The production and growth of crops may be impacted if such contaminated effluent is used for irrigation (<xref ref-type="bibr" rid="B162">Rahman et al., 2018</xref>). For the treatment of wastewater from the dye industry, advanced oxidation processes, membrane filtration, microbial technologies, bio-electrochemical degradation, and photocatalytic degradation have been documented (<xref ref-type="bibr" rid="B66">Gao et al., 2023</xref>; <xref ref-type="bibr" rid="B79">Iqbal et al., 2023</xref>; <xref ref-type="bibr" rid="B212">Verma et al., 2023</xref>). In addition to assisting in the treatment of wastewater, innovative techniques including microalgae cultivation, biobased adsorbents, and membrane technologies also aid in the recovery of dyes and pigments that may be reused and recycled sustainably (<xref ref-type="bibr" rid="B60">Eskikaya et al., 2023</xref>; <xref ref-type="bibr" rid="B222">Xiong et al., 2023</xref>). Wastewater phytoremediation represents a promising circular economy-based approach for wastewater reclamation, resource recovery, and generation of value-added products. With unique health benefits, natural pigments are now in high demand in the market, as natural colouring agents in food industry sector (<xref ref-type="bibr" rid="B38">Christaki et al., 2015</xref>; <xref ref-type="bibr" rid="B216">Villaro et al., 2021</xref>). Phycobiliproteins are photosynthetic pigments found in the microalgae, and are widely used in the food, cosmetic, and pharmaceutical industries (<xref ref-type="bibr" rid="B195">Sun et al., 2023</xref>). While microalgae are seen to be a promising contender for the production of natural pigments and the demand for natural dyes is rising, the high costs associated with large-scale systems necessitate the use of enormous amounts of water and nutrients. It also makes it more difficult to produce and market these bioproducts. Natural pigments&#x2019; production from microalgal culture grown over wastewater as growth medium has been recently foreseen as a potential solution to both environmental pollution and high cost production of pigments (<xref ref-type="bibr" rid="B18">Blanco-Vieites et al., 2023</xref>). This approach will remediate the wastewater and produce natural dyes and pigments (<xref ref-type="bibr" rid="B222">Xiong et al., 2023</xref>). Further, the algal biomass may be utilized to produce biogas, biofertilisers, and other byproducts. <xref ref-type="bibr" rid="B8">Arashiro et al. (2020)</xref> cultivated microalgae consortium on industrial wastewater for the recovery of phycobiliproteins aiming to bioremediation of wastewater and sustainable production of value-added compounds. The high recovery rates were observed for Phycocyanin (103&#xa0;mg/g dry wt), allophycocyanin (57&#xa0;mg/g dry wt), and phycoerythrin (30&#xa0;mg/g dry wt), from algal biomass respectively. Furthermore, microalgae culture successfully removed the COD, inorganic nitrogen, and phosphate up to 98%, 94%, and 100%. <xref ref-type="bibr" rid="B190">Stepnowski et al. (2004)</xref> used fish scale waste as a natural adsorbent for the recovery of astaxanthin, a carotenoid pigment from seafood industry wastewater. Astaxanthin is widely utilised as a coloration agent for farmed salmonids, including the natural or synthetic pigment in the fish diet (<xref ref-type="bibr" rid="B74">Hatlen et al., 1995</xref>). The pigment is also considered in medical and biomedical studies and applications due to its biological function as a vitamin A precursor and its high antioxidative effects. The results show that astaxanthin bound onto the scales-based adsorbent was 88%&#x2013;95% of the total sorbed pigment in its esterified form. The maximum loading capacity of astaxanthin onto the scales was 362&#xa0;mg/kg dry wt.</p>
</sec>
<sec id="s3-4">
<title>3.4 Recovery of enzymes</title>
<p>Most commercial enzymes are derived from bacterial biomass. Additionally, they are extracted of other fungi, including yeast made in a commercial fermentation method. Specific culture mediums are used in the synthesis of industrial enzymes. These culture media are capable of offering all the nutrients required for microbial growth, consolidation, and purification. By disrupting the biomass, enzymes are extracted, then combined with stabilisers to create various solid/liquid products that can be sold. Particularly synthetic culture mediums are among the most expensive components of commercial enzyme synthesis, accounting for approximately to 30%&#x2013;40% of the overall cost of production. Therefore, cost-effective approaches to producing hydrolytic microbial biomass, avoiding the need for synthetic growth media, might offer significant commercial advantages for industrial enzyme production.</p>
<p>
<xref ref-type="bibr" rid="B37">Cheng et al. (2015)</xref> studied how to extract an enzyme called polyphenol oxidase (PPO) from potato starch wastewater. PPO has many uses but is expensive to produce commercially, so it is not used as much as it could be. The researchers adjusted the pH of the wastewater to 3.5 to cause a chemical reaction that would cause a protein called PPO to separate from the wastewater. They then added 50% acetone to the wastewater to cause a different chemical reaction that would cause a different protein called beta-amylase to separate from the wastewater. Finally, they added 80% acetone to the wastewater to cause a reaction that would cause a type of carbohydrate called sporamins to separate from the wastewater. After the acetone was recovered, the researchers were able to obtain 4.3 &#xd7; 105 units of PPO, 4.0 &#xd7; 106 units of beta-amylase, 8.70&#xa0;g of sporamins, and 20.2&#xa0;g of SMNs from 1&#xa0;kg of sweet potato wastewater. <xref ref-type="bibr" rid="B108">Libardi et al. (2017)</xref> studied the possibility of using wastewater from toilets containing toilet paper as a source of cellulose for producing cellulases. Using wastewater as a source of cellulose makes it possible to produce an added-value product while also reducing the pollution charge of the wastewater by consuming it as a source of carbon and nutrients. In another study <xref ref-type="bibr" rid="B107">Libardi et al. (2019)</xref> conducted a study to produce cellulase enzymes from domestic wastewater. They used <italic>Trichoderma harzianum</italic> as the culture medium and tested three bioreactor systems; a bubble column bioreactor (BCB), column-packed bed reactor (CPBR), and stirred tank reactors (STR). The BCB system was the most successful, producing the highest cellulase activity and productivity of 31&#xa0;UFP/mL and 645&#xa0;UFP/mL.h without needing immobilisation. The fermented broth was then microfiltered and ultrafiltered, resulting in a cellulase recovery of 73.5% using a 30&#xa0;kDa membrane, which increased the activity concentration by 4.23 times. Additionally, the study found that the COD and nitrogen concentration in the wastewater was reduced by 81.37% and 52.9%, respectively. The production of cellulase enzymes from domestic wastewater and the subsequent development of an added-value process with minimal environmental impact are both highly anticipated opportunities. Moreover, accounting about 30% of the global enzyme market, amylase is a vital industrial enzyme. (<xref ref-type="bibr" rid="B68">Gomez-Villegas et al., 2021</xref>). It has significant role in multiple industries, such as pharmaceuticals, textiles, chemicals, paper, and food. <xref ref-type="bibr" rid="B232">Yusree et al. (2022)</xref> used a Liquid biphasic system (LBS) to extract and purify a type of amylase called beta-amylase from sweet potato slurry. This LBS is a green extraction technology that combines polyethylene glycol and citrate to separate the beta-amylase from the sweet potato slurry. The results demonstrate an upward trend in recovery yield (78.24%), purification factor (3.5087), and selectivity when salt and polymer concentrations upsurged.</p>
</sec>
</sec>
<sec id="s4">
<title>4 Valorisation of wastewater and sludge</title>
<sec id="s4-1">
<title>4.1 Production of biofuels</title>
<p>Wastewater and sewage sludge are no longer considered a waste because it may be used to recover, recycle and produce valuable products (<xref ref-type="bibr" rid="B185">Singh et al., 2022</xref>). Biofuels like biogas, biodiesel, biohydrogen, bioethanol, etc., can be produced using wastewater and sludge. Anaerobic digestion methods are already being used on an industrial scale to effectively valorise the sludge as these provide various social and environmental benefits in addition to green energy and manure (<xref ref-type="bibr" rid="B152">Pasciucco et al., 2023</xref>). Biogas production from organic waste helps reduce the negative impacts associated with organic wastes in landfills causing groundwater and soil pollution, the emission of air pollutants such as dioxins and furans, methane, and more substantial greenhouse gases. However, the amount of methane gas produced from sludge by anaerobic digestion is lower than other types of organic waste. Thus, pretreatment and co-digestion contribute to improving the degradability of organic matter and methane production potential of sludge, respectively (<xref ref-type="bibr" rid="B98">Kumar et al., 2017</xref>; <xref ref-type="bibr" rid="B104">Lewis et al., 2017</xref>; <xref ref-type="bibr" rid="B58">Elalami et al., 2019</xref>; <xref ref-type="bibr" rid="B226">Yadav et al., 2023</xref>).</p>
<p>Municipal wastewater sludge, pulp, and paper wastewater containing cellulose combined with lignin could be used as raw materials for bioethanol production (<xref ref-type="bibr" rid="B21">Bon et al., 2022</xref>). Using cellulases enzymes from <italic>Trichoderma reesei</italic>, cellulose components are hydrolyzed into sugar (saccharification), and the resulting sugar is used as a raw ingredient for the production of bioethanol by <italic>Saccharomyces cerevisiae</italic> (<xref ref-type="bibr" rid="B57">el-Zawawy et al., 2011</xref>). Further, in a study led by <xref ref-type="bibr" rid="B53">Dufreche et al. (2007)</xref>, Lipids were used as a cheap source of raw material for the production of biodiesel after being extracted from municipal wastewater sludge using solvents such n-hexane, methanol, acetone, and supercritical CO<sub>2</sub>. Additionally, dried sludge was reported to be used to produce 6.23% biodiesel using <italic>in situ</italic> transesterification process (<xref ref-type="bibr" rid="B53">Dufreche et al., 2007</xref>). Owing to its clean product and high energy production (122&#xa0;kJ/g), hydrogen is an attractive energy source. Water electrolysis, steam reforming of hydrocarbons, and auto-thermal processes are well-known ways of producing hydrogen gas, but these are expensive due to high energy needs. Environment-friendly anaerobic biohydrogen fermentation from organic wastes is gaining popularity because of its minimum waste and bioenergy produced. A low hydrogen-yielding rate is essential in biohydrogen synthesis from the garbage. Several aspects must be addressed to maximise hydrogen generation throughout the fermentation process, such as minimising hydrogen loss to hydrogen-consuming anaerobes like methanogens. Other elements, such as inoculum, substrate, temperature, nitrogen sparging, and early startup, have all been investigated by researchers to increase hydrogen generation (<xref ref-type="bibr" rid="B106">Li et al., 2008</xref>; <xref ref-type="bibr" rid="B198">Tang et al., 2008</xref>). However, biofuel production from wastewater and sludge is still in its infancy. Therefore, further large-scale studies are required to realise the benefits of this new technology at an industrial scale.</p>
</sec>
<sec id="s4-2">
<title>4.2 Production of biopolymers</title>
<p>To build a sustainable wastewater treatment facility, resource recovery from wastewater sludge is emphasised. Wastewater sludge is thought of as a viable source for recovering high-value products like biopolymers and biofertilizers. (<xref ref-type="bibr" rid="B178">Sharma et al., 2022</xref>). Activated sludge is a matrix of microbial cells entrenched in an extracellular polymeric substance (EPS) released by microbes. About 10%&#x2013;40% dry weight of total activated sludge accounts for the EPS. EPS is considered as rich source of polysaccharides, nucleic acid, lipids, proteins, and humic acids (<xref ref-type="bibr" rid="B14">Basuvaraj et al., 2015</xref>; <xref ref-type="bibr" rid="B20">Boltz et al., 2017</xref>). In a recent study, EPS mined from wastewater sludge has been characterised to measure physical and chemical properties (<xref ref-type="bibr" rid="B110">Lin et al., 2013</xref>; <xref ref-type="bibr" rid="B111">2018</xref>; <xref ref-type="bibr" rid="B155">Pronk et al., 2015</xref>). The matrix&#x2019;s biopolymers provide a distinctive structure that can be salvaged to create potentially useful biomaterials. (<xref ref-type="bibr" rid="B179">Sheng et al., 2010</xref>; <xref ref-type="bibr" rid="B139">More et al., 2014</xref>). For instance, alginate-like extracellular polymers (ALE) can potentially be extracted from aerobic granular sludge (AGS) (<xref ref-type="bibr" rid="B166">Rehm, 2010</xref>; <xref ref-type="bibr" rid="B109">Lin et al., 2015</xref>; <xref ref-type="bibr" rid="B111">Lin et al., 2018</xref>). Due of their widespread use in the food, paper, medicinal, construction, and textile industries, the recovery of these ALE polymers from sludge is receiving a lot more attention lately (<xref ref-type="bibr" rid="B93">Kim et al., 2020</xref>; <xref ref-type="bibr" rid="B105">Li et al., 2021</xref>).</p>
<p>By using solution casting, EPS recovered from surplus granular sludge was successfully integrated into polyvinyl alcohol (PVA) (<xref ref-type="bibr" rid="B92">Kim et al., 2022</xref>). Polyvinyl alcohol (PVA) is a type of material that has many uses. It is known for its strong resistance to chemicals and its physical qualities, making it useful for various applications. These applications include textile production, paper sizing, and the manufacture of filaments (<xref ref-type="bibr" rid="B138">Mohareb et al., 2011</xref>). In the building industry, it is common to use a certain substance as a binding and thickening agent for latex paints and seals. This substance helps to hold the paint and seal together, making it thicker and more durable (<xref ref-type="bibr" rid="B130">Marten, 2002</xref>) and as a modifier to improve the strength and durability of the material in fibre reinforcement and cement-based composite materials (<xref ref-type="bibr" rid="B202">Thong et al., 2016</xref>).</p>
</sec>
<sec id="s4-3">
<title>4.3 Production of biofertilisers</title>
<p>The valorisation of waste into byproducts by applying a circularity principle is a central and essential issue to foster sustainable economic development. In this context, municipal wastewater has a high potential for nutrient valorisation and sustainable production chain development. An example is sewage sludge as a source of nutrients for crops (<xref ref-type="table" rid="T5">Table 5</xref>). Dewatered sludge containing nutritional and organic content is utilised as agricultural fertiliser. Sludge&#x2019;s organic matter, nitrogen, and phosphorus content promotes plant development and improves agricultural soil quality. Majority of farmers from West African and South Asian countries view untreated sewage as a useful fertiliser, despite the fact that using untreated sludge as a fertiliser is unacceptable (<xref ref-type="bibr" rid="B40">Cofie et al., 2005</xref>; <xref ref-type="bibr" rid="B209">Verhagen et al., 2012</xref>). Farmers use untreated dried sewage as free fertiliser, including nitrogen (322&#xa0;kg&#xa0;N/ha/year) and phosphorus (64&#xa0;kg&#xa0;P/ha/year). The chemical composition and characteristics of untreated and digested sewage sludge are shown in <xref ref-type="table" rid="T1">Table 1</xref>. The demand for fertilisers for agricultural production is increasing due to the world population (<xref ref-type="bibr" rid="B120">Mahmoud et al., 2022c</xref>). At current demand for nitrogen is more than 130 million tonnes, and the demand for phosphorus is about 16 million tonnes. Recovery of nutrients from wastewater sludge could meet the local requirement of fertilisers for agricultural production (<xref ref-type="bibr" rid="B62">FAO, 2008</xref>; <xref ref-type="bibr" rid="B61">FAO, 2012</xref>; <xref ref-type="bibr" rid="B12">Balasubramanian and Tyagi, 2017</xref>).</p>
<table-wrap id="T5" position="float">
<label>TABLE 5</label>
<caption>
<p>The chemical composition and characteristics of untreated and digested sewage sludge.</p>
</caption>
<table>
<thead>
<tr>
<th align="left">Chemical composition</th>
<th align="left">Untreated sludge</th>
<th align="left">Digested sludge</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Total dry solids (TS), %</td>
<td align="left">2.0&#x2013;8.0</td>
<td align="left">6.0&#x2013;12.0</td>
</tr>
<tr>
<td align="left">Nitrogen, (N, % of TS)</td>
<td align="left">1.5&#x2013;4</td>
<td align="left">1.6&#x2013;6.0</td>
</tr>
<tr>
<td align="left">Phosphorus, (P<sub>2</sub>O<sub>5</sub>, % of TS)</td>
<td align="left">0.8&#x2013;2.8</td>
<td align="left">1.5&#x2013;4.0</td>
</tr>
<tr>
<td align="left">Potash, (K<sub>2</sub>O, % of TS)</td>
<td align="left">0.0&#x2013;1.0</td>
<td align="left">0.0&#x2013;3.0</td>
</tr>
<tr>
<td align="left">Protein, (% of TS)</td>
<td align="left">20&#x2013;30</td>
<td align="left">15&#x2013;20</td>
</tr>
<tr>
<td align="left">pH</td>
<td align="left">5.0&#x2013;8.0</td>
<td align="left">6.5&#x2013;7.5</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Recent advancement in sewage sludge treatment technology allows the recovery of nutrients such as nitrogen and phosphorus. These recovered nutrients can be utilised as bio-fertilisers by replacing synthetic fertilisers (<xref ref-type="bibr" rid="B75">Herzel et al., 2016</xref>). <xref ref-type="bibr" rid="B164">Rebah et al. (2002)</xref> and <xref ref-type="bibr" rid="B183">Singh et al. (2013)</xref> conducted experiments to explore the utilisation of sludge as a medium to grow <italic>Rhizobium</italic> bacteria which has been applied as a bio-fertiliser directly onto the soil. <xref ref-type="bibr" rid="B150">Paliya et al. (2019)</xref> also experimented on sludge ash. They concluded that sludge ash could be utilised as a sustainable raw material to produce bio-fertilisers. This conclusion was made possible by incorporating it in a definite amount with the inoculum of different microbial species. Industrial and municipal wastewater sludge (primary and secondary sludge from wastewater treatment plants) was used as a raw material to grow various rhizobial strains such as <italic>Sinorhizobium meliloti,</italic> and <italic>Rhizobium leguminosarum bv. viciae, Bradyrhizobium japonicum, and Bradyrhizobium elkanii</italic>. Among all these strains <italic>S. meliloti</italic> strain grew well compared to other strains in the sludge. Sludge characteristics also influenced bacterial growth, cell yield, and fermentation time. Suspended solid particles increased in sludge significantly reduced the oxygen transfer and the rhizobial growth (<xref ref-type="bibr" rid="B165">Rebah et al., 2001</xref>). <xref ref-type="bibr" rid="B169">Romero-Garcia et al. (2022)</xref> used wastewater sludge as a raw material to form a microalgal bio fertiliser high-pressure homogenisation process. This process converts the microalgal biomass produced in the wastewater treatment plant into a bio-fertiliser used in agriculture to improve crops and reduce traditional fertilisers. Subsequently, progress toward a sustainable food system for the twenty-first century under the United Nations&#x2019; 2030 Agendas of Sustainable Development Goals. Microalgae grown in wastewater can be utilised as a bio-fertiliser for soil amendment. Microalgal biomass can enhance soil nitrogen and phosphorus levels and numerous other plant-required trace elements (Ca, K, Fe, and Mn). When combined with soil-based phosphorus-solubilizing organisms, microalgal fertilisers have boosted phosphorus release in the soil. The landfill leachate biomass possesses great potential to generate biofertilizers (<xref ref-type="bibr" rid="B203">Tighiri and Erkurt, 2019</xref>; <xref ref-type="bibr" rid="B188">Solovchenko et al., 2021</xref>). A study led by <xref ref-type="bibr" rid="B208">Umamaheswari and Shanthakumar (2021)</xref>, reported 30% increase in the dry weight and biochemical content of wheat crop upon input of filamentous microalgae strains as bio-fertilizers. Microalgae and bacteria symbiotically transform organic and inorganic compounds into smaller biomolecules that plants can absorb, making them efficient biofertilizers (<xref ref-type="bibr" rid="B63">Ferreira et al., 2019</xref>).</p>
</sec>
<sec id="s4-4">
<title>4.4 Production of biopesticides</title>
<p>Biological agents might be used to manage and target insects in a specific and selective manner, reducing the need for hazardous chemical pesticides while simultaneously improving environmental quality and human health (<xref ref-type="bibr" rid="B172">Sabbahi et al., 2022</xref>). To attain a high yield of biopesticide manufacturing, wastewater sludge has been proven an economically viable solution (<xref ref-type="bibr" rid="B28">Butu et al., 2022</xref>). Wastewater sludge is considered a global problem, and its sustainable management via value addition is an efficient alternative to other disposal methods, such as landfilling and incineration (<xref ref-type="bibr" rid="B173">Sachdeva et al., 2000</xref>). <xref ref-type="bibr" rid="B207">Tyagi et al. (2002)</xref> achieved the production of <italic>Bacillus thuringiensis, a</italic> potential biopesticide by using both industrial and municipal wastewater sludge as raw materials. Both municipal and industrial wastewater sludge has been proven viable for biopesticide synthesis; however, the entomotoxicity potential of the biopesticide produced was found to rely on the nutrient composition of the sludge (<xref ref-type="bibr" rid="B207">Tyagi et al., 2002</xref>; <xref ref-type="bibr" rid="B229">Yezza et al., 2005</xref>). Utilisation of sludge waste for Bt biopesticide has potential to can considerably cut the production costs while contributing significantly to sustainable sludge usage and management. <xref ref-type="bibr" rid="B23">Brar et al. (2006)</xref> used submerged fermentation in the bioconversion of wastewater sludge into Bt-based biopesticides. However, extraction of microorganism was found to be challenging due to the low concentration of products in submerged fermentation, resulting in complex downstream processing (<xref ref-type="bibr" rid="B23">Brar et al., 2006</xref>) and necessitating pricy and high end equipments such as a high-speed cooling centrifuge and spray dryer (el-<xref ref-type="bibr" rid="B17">Bendary, 2006</xref>). In contrast to traditional submerged fermentation, solid-state fermentation technology has several biotechnological advantages, including low to medium cost and energy consumption, little effluent output, and decent product stability (<xref ref-type="bibr" rid="B151">Pandey, 2003</xref>; <xref ref-type="bibr" rid="B76">Holker and Lenz, 2005</xref>; <xref ref-type="bibr" rid="B186">Singhania et al., 2009</xref>).</p>
<p>Therefore, producing Bt-based biopesticides from sludge or wastewater could be a novel and ingenious way to clean up the environment and an addition to the path for commercialising affordable biopesticides (<xref ref-type="bibr" rid="B205">Tiwari and Awasthi, 2022</xref>). Biopesticide production from the starch industry wastewater and sludge has been thoroughly studied including pretreatment, medium amelioration agents, optimising process parameters, scaleup, and formulation and development studies (<xref ref-type="bibr" rid="B207">Tyagi et al., 2002</xref>; <xref ref-type="bibr" rid="B24">Brar et al., 2004</xref>). Wastewater sludge and starch industry wastewater proved to be very effective media for the cultivation of Bt (<xref ref-type="bibr" rid="B144">Ndao et al., 2021</xref>). The shift from linear to circular economies, in which the value of resources, materials, and products is retained throughout the value chain, is an essential step towards establishing a more sustainable, waste free, and competitive economy. <italic>Bacillus thuringiensis</italic> (Bt) is the most frequently employed microbial biopesticide, producing crystal proteins with biopesticide activity against insects from the orders Coleoptera, Lepidoptera, Diptera, Hymenoptera, Hemiptera, and Orthoptera, as well as phytopathogenic nematodes and terrestrial gastropods (<xref ref-type="bibr" rid="B127">Malovichko et al., 2019</xref>). The sporulation process is linked to the synthesis of this protein (Cry protein) (<xref ref-type="bibr" rid="B33">Chandler et al., 2011</xref>). Nowadays, 90% of commercialised biopesticides are produced from this entomopathogenic bacteria. These biopesticides are more effective to target pests even in a small dose, and are fast decomposable without leaving hazardous residues as compare to chemical conventional pesticides (<xref ref-type="bibr" rid="B97">Kumar and Singh, 2015</xref>; <xref ref-type="bibr" rid="B47">Damalas and Koutroubas, 2018</xref>; <xref ref-type="bibr" rid="B227">Yadav et al., 2022</xref>). Biopesticides, bioherbicides, biofertilizers, bioplastics, and enzymes derived from wastewater sludge are low-cost biological alternatives that can compete with chemicals or other cost-intensive biological goods in present market. The bioconversion of wastewater sludge into biopesticides or other bio-control agents, has been contemplated, with promising results. <italic>Trichoderma, Rhizobium,</italic> and <italic>Bacillus</italic> sp. are the more capable of growing in wastewater and wastewater sludge and producing microbial derivatives utilised in biocontrol and bio-bleaching processes. (<xref ref-type="bibr" rid="B211">Verma et al., 2007a</xref>; <xref ref-type="bibr" rid="B210">b</xref>; <xref ref-type="bibr" rid="B192">Subramanian et al., 2008</xref>). Unfortunately, <italic>Trichoderma</italic> sp. has not been widely used due to lack of economically feasible procedures, as most existing techniques uses expensive raw ingredients and have lower spore production, which is critical for their performance as a bio-control agents. <xref ref-type="bibr" rid="B5">Alam and Fakhrul-Razi (2003)</xref> discussed the use of <italic>Trichoderma</italic> sp. for wastewater and wastewater sludge treatment to decompose organic matter and hazardous organic compounds, but they did not use the waste as a raw material for the manufacturing of value-added products. According to <xref ref-type="bibr" rid="B211">Verma et al. (2007a)</xref>, <xref ref-type="bibr" rid="B210">Verma et al. (2007b)</xref>, <italic>Trichoderma viride</italic> is a promising bacterium that forms laccases in wastewater sludge and has the ability to breakdown or detoxify organic contaminants such as BPA. Cells of <italic>Rhizobium</italic> sp. and <italic>Sinorhizobium meliloti</italic> are utilised as microbial inoculants in leguminous cultures and as biological control agent in agricultural crops. Laccases generated by <italic>S. meliloti</italic> have the capacity to breakdown or detoxify organic chemicals, particularly phenolic groups contained in wastewater sludge, while also bio-converting wastewater sludge into value-added products (<xref ref-type="bibr" rid="B170">Rosconi et al., 2005</xref>). <italic>Bacillus</italic> sp. can generate enzymes that breakdown organic contaminants in wastewater and wastewater sludge, such as oxidases, dehydrogenases, and peroxidases. <italic>Bacillus thuringiensis</italic> generates tyrosinases, which may breakdown phenolic substances (<xref ref-type="bibr" rid="B52">Donova et al., 2005</xref>; <xref ref-type="bibr" rid="B158">Quan et al., 2005</xref>). Biopesticides based on <italic>B. thuringiensis</italic> have been demonstrated to breakdown an Endocrine disrupting chemical, Dimethyle patholate, concurrently with biopesticide synthesis (<xref ref-type="bibr" rid="B25">Brar et al., 2009</xref>). Consequently, value-added product-generating microorganisms like <italic>Rhizobium</italic> sp., <italic>Bacillus</italic> sp., and <italic>Trichoderma</italic> sp. have an enzyme system that can efficiently break down organic chemicals (<xref ref-type="bibr" rid="B137">Mohapatra et al., 2010</xref>). Several researchers have utilised SSF technology to create Bt-derived biopesticides from soy waste, sugar beet pulp, sesame meal, wastewater sludge and wasted mushrooms. <xref ref-type="bibr" rid="B234">Zhang et al. (2013)</xref> achieved a successful fermentation procedure with 35&#xa0;kg of fermentation media that was mostly made of kitchen garbage. When the spore count was increased from 4 to 8&#xa0;kg, the ultimate spore counts increased. When the procedure was expanded up to 35&#xa0;kg, spore output reduced marginally. When 40&#xa0;kg of substrate was used, this value significantly reduced (from 9.6108&#xa0;CFU/g to 6.4106&#xa0;CFU/g), owing to insufficient ventilation and heat removal as the primary hypothetic factors. The feasibility of utilising digestate as a fermentation substrate for <italic>B. thuringiensis</italic> var kurstaki (Btk) culture and spore generation was investigated by <xref ref-type="bibr" rid="B168">Rodriguez et al. (2019)</xref>. This proof of concept demonstrated that the procedure was achievable at lab and bench-scale (10-L), with scanning electron microscopy pictures confirming the existence of protein crystals. Nevertheless, scaling up to 22 and 100-L proved that Bt was unable to develop, revealing only its capacity to sporulate. As a result, the procedure for producing biopesticide must be improved to improve Bt&#x2019;s capacity to colonise solid material at these sizes. A successful operational strategy for <italic>B. thuringiensis</italic> spore production was achieved using a digestate-biowaste mixture (62.5%&#x2013;37.5%, wet weight basis) and a novel aeration strategy divided into two stages: a micro aeration phase during the first hours of fermentation, followed by a high-rate aerated period after 22&#xa0;h. Under these circumstances, Bt spore production ranged between 5 &#xd7; 10<sup>7</sup> and 1.5 &#xd7; 10<sup>8</sup> spores/g dry matter, with a maximum production yield of 5&#x2013;7.3 spores/CFU. Biodegradability has emerged as a critical issue in the feasibility of both Bt growth and two-stage aeration strategies. This research established the operational framework for carrying out the developed method on a demonstration scale (<xref ref-type="bibr" rid="B132">Mejias et al., 2020</xref>). Therefore, using sludge for biopesticide production will minimise the environmental problem of sludge disposal and the problems encountered with chemical pesticides.</p>
</sec>
</sec>
<sec id="s5">
<title>5 Life cycle assessment and techno-economic analysis</title>
<p>The term &#x201c;life cycle assessment&#x201d; (LCA) refers to the process of measuring a product&#x2019;s environmental impact throughout the course of its whole life cycle, from conception to disposal. LCA is a methodical process that uses ISO 14040 (2006) standards to translate a system&#x2019;s inputs and outputs into corresponding environmental consequences. LCA is divided into four stages&#x2014;goal and scope definition, data acquisition and life cycle inventory, life cycle impact assessment, and outcome interpretation (<xref ref-type="bibr" rid="B45">Cortes et al., 2020</xref>).</p>
<p>
<xref ref-type="bibr" rid="B174">Sangma and Chalie (2023)</xref> performed LCA and techno-economic analysis (TEA) to demonstrate that wastewater treatment with microalgae can significantly lessen adverse environmental effects in comparison to conventional methods. The system also provided the benefit of low operating costs, scope for nutrient recovery, waste valorisation into value added products, and the ability to reduce emissions by absorbing CO<sub>2</sub> from flue gases. A more comprehensive environmental assessment was also recommended in the review by <xref ref-type="bibr" rid="B102">Lee and Jepson (2021)</xref> which compared the LCA studies of RO against emerging technologies, such as forward osmosis and capacitive deionization. This review highlighted the trade-off between carbon emissions and chemical treatment and concluded emerging technologies that aim to reduce energy consumption have the potential to increase other environmental burdens such as chemical usage; <xref ref-type="bibr" rid="B73">Hand and Cusick (2021)</xref> performed LCA for electrochemical oxidation (EO) technology and reported that EO is a promising technique for wastewater treatment and purification, but it may pose unintended negative consequences on the environment due to the consumption of resources and energy during the electrodes manufacturing and operational stages. <xref ref-type="bibr" rid="B193">Sun et al. (2023)</xref> quantitatively assessed the LCA of the EO method&#x2019;s environmental effects from the lab to the industrial scale. As per their findings EO was found to be efficient in destroying organic pollutants in wastewater, however, the benefits were outweighed by the environmental burdens related to the manufacturing of anode materials, use of electrolytes, and energy consumption during various operational stages. This obligated the attention to the LCA by taking reactor design, anode materials, electrolyte, and flow pattern into consideration, as well as demanded decentralized location with a significant share of renewable power source and stringent contamination control policies for WWTPs.</p>
<p>
<xref ref-type="bibr" rid="B86">Juneja and Murthy (2017)</xref> applied an engineering course model on a renewable diesel (RD) production facility with a processing capacity of 60&#xa0;Mgal wastewater/day to conduct a TEA of RD production on a commercial scale. Algal RD yields were estimated as 10.18&#xa0;MML/year, with a production cost per RD of $1.75. According to the LCA, the manufacturing of RD resulted in GHG emissions that were 6.2 times lower than those of regular diesel. Sensitivity study suggested that using high lipid algae or expanding the production facility could lower the cost of producing ethanol. The long-term viability of RD in an ecologically friendly path was found to be helped by the integrated TEA and LCA evaluations. <xref ref-type="bibr" rid="B67">Gholkar et al. (2021)</xref> used microalgal biomass grown on steel mill wastewater to perform TEA and LCA on hydrogen and methane generation, and they found life cycle climate change impact was 7.56&#xa0;kg CO<sub>2</sub> eq./kg hydrogen generated, which was 36.47% less than steam reforming of methane. It was not economically possible to produce methane. Yet, with a life cycle climate change impact of 1.18&#xa0;kg CO2 eq./kg methane generated, it was more environmentally friendly. Sensitivity analysis was done to find areas where costs and life cycle impacts could be further reduced.</p>
<p>
<xref ref-type="bibr" rid="B141">Mu et al. (2014)</xref>, evaluated the environmental performance of wastewater based algal biofuels and reported that environmental performance of wastewater based algal biofuels was much better than freshwater based algal biofuels however, the characteristics of wastewater and conversion technologies played key role in performance and LCA. <xref ref-type="bibr" rid="B9">Arashiro et al. (2022)</xref> conducted LCA to compare microalgae systems for wastewater treatment and bioproducts for treating industrial wastewater (food sector) and urban wastewater, with the goal of recovering bioproducts and bioenergy. Findings showed that microalgal based WWT systems assisted bioproduct recovery can minimise the environmental impacts up to five times in comparison to conventional systems owing to the lower chemical consumption for microalgae cultivation. Because of its higher quality compared to urban wastewater, which also permits the growing of a single species of microalgae, food industry effluent emerged as the most efficient set-up for the recovery of bioproducts from microalgae treated wastewater. In conclusion, the LCA advocated the microalgae wastewater treatment systems a promising alternative for wastewater treatment and nutrient recovery. <xref ref-type="bibr" rid="B32">Castro et al. (2020)</xref> used LCA to compare the environmental effects of producing microalgae biomass-based phosphate biofertilizer to triple superphosphate. Phosphorus recovery was made from the wastewater of the meat processing sector using microalgae. Climate change impact was found to be 3.17&#xa0;kg CO<sub>2</sub>eq. Microalgae biofertilizer had higher environmental effect than conventional fertilizer in all impact categories. To get around this, a seamless set-up was established that used photovoltaic panels as the power source and a drying bed for biomass drying instead of thermal drying; <xref ref-type="bibr" rid="B191">Styles et al. (2018)</xref> used LCA to evaluate the production and usage of digestate biofertilizer (DBF) derived from liquid digestate (LD), accounting for SFS efficacy, with the conventional management of LD from food waste. More judicious use of nutrients in the DBF product could result in benefits in terms of environment and economy by preventing methane, nitrogen oxides, and ammonia gas emissions from LD and SFS. They came to the conclusion that DBF extraction was economically advantageous and sustainable after averaging these results against larger environmental loadings.</p>
<p>Henceforth, the use of LCA is extremely helpful in determining the energy products and co-products which will demonstrate higher economic viability and environmental performance (<xref ref-type="bibr" rid="B41">Collet et al., 2015</xref>). Since there is a large variability in assessments done by multiple studies, <xref ref-type="bibr" rid="B159">Quinn and Davis (2014)</xref> emphasized the need for integrated Resource assessment (RA), Techno economic analysis (TEA), and LCA constructed on a foundation of experimentally validated technological system models.</p>
</sec>
<sec id="s6">
<title>6 Challenges in resource recovery and wastewater valorisation</title>
<p>Wastewater valorisation is a potential method to reuse and recycle water and nutrients for economic generation and environmental protection. However, the current status and technological bottlenecks still inhibit the effective use of this concept. Different countries have different obstacles that they need to overcome. The difficulty of these obstacles can vary depending on the situation.<list list-type="simple">
<list-item>
<p>1. The main challenge with Membrane separation technology is figuring out which membrane is best suited for the desired outcome. It is important to choose the right membrane suitable for the process to be successful. To compete with the existing conventional technologies, membrane clogging and fouling are still considered the primary stumbling blocks for membrane-based separation.</p>
</list-item>
<list-item>
<p>2. Enzymatic catalysis and recovery of products depend upon the physicochemical properties of wastewater, such as pH; since enzymes are heat and pH labile and are easily denatured in highly basic or acidic solutions, this may limit their functioning, increasing the cost of treatment and valorisation.</p>
</list-item>
<list-item>
<p>3. Microalgae-based WWT is one of the most optimistic technologies for waste&#x2019;s advanced treatment and nutrient recovery. Most studies have been conducted at pilot or bench scale and under controlled conditions. Thus, cultivation under outdoor conditions and scaling up of reactors are still needed to evaluate the direct interferences on processes involved in the valorisation of wastewater. However, large-scale cultivation under outdoor conditions is still a challenge.</p>
</list-item>
<list-item>
<p>4. Economic, technical, political, institutional, and social challenges are frequently encountered in implementing small and large-scale valorisation operations.</p>
</list-item>
<list-item>
<p>5. Another big challenge is the lack of trust and awareness of recycled/recovered and valorised products. Many consumers may be skeptical about the quality of valorised and recycled products. The consumer may perceive the products based on the Circular economy as high-risk and uncertain.</p>
</list-item>
<list-item>
<p>6. Additionally, if the price of non-circular products is higher than circular/valorised products, then taxation on virgin resources (resources that have not been used before) could be used to make the circular/valorised products more attractive to consumers. Thus, taxation on virgin resources might provide an advantage.</p>
</list-item>
<list-item>
<p>7. A key barrier often presents unavailable and irregular infrastructure. in developing countries, these systems and services are often not up to the same standards as in more developed countries.</p>
</list-item>
</list>
</p>
</sec>
<sec id="s7">
<title>7 Conclusion and recommendations</title>
<p>Adopting the circular economy concept is crucial to meet global challenges. These global challenges include increasing demand for water supply, water scarcity, and declining non-renewable resources. Sludge and wastewater are no longer considered to be trash, but rather a source of valuable products that can benefit environmentally and social-economically. In this review, authors have explained the wastewater and sludge valorisation for multiple aspects such as water resource management, environmental protection, resource recovery, and generation of value-added products. With the aid of the cutting-edge technologies, wastewater can be efficiently treated, resulting in effluents of a calibre that meets the standards of industry and agriculture. Water reuse is not the only way to value wastewater. Recognizing that wastewater contains a variety of valuable resources that can be recovered is vital. In order to reduce pollution, protect the environment, wastewater treatment processes must recover nutrients. Traditional approaches by themselves are insufficient to extract nutrients in high quantities and of desired quality until they are united with membrane technology. The use of the unique hybrid systems in nutrient recovery is highlighted. To increase the technological viability and lower operational expenses, further work must still be done to improve the recovery system&#x2019;s usability. Finally, apart from this, governments should put into place relevant legislation, policies, and regulations to support and encourage nutrient recovery strategies.</p>
<p>Nutrients such as phosphorous, nitrogen, phenolic compounds, antioxidants, vitamins, proteins, enzymes, and other value-added products can be potentially recovered from wastewater from various industrial sectors. High-end and novel separation and purification technologies, such as membrane technology, enzyme-mediated separation, chromatography, microalgae cultivation, and novel adsorbents, enable efficient recovery of nutrients and treatment of wastewater. Various strategies can be applied to valorise this waste related to excess sludge produced during wastewater treatment. Value-added substances made from anaerobic sludge digestion, such as bio-fertilizers, bioplastics, biofuels, and biocompost, are already used extensively in large-scale processes. Yet, incorporating the water sector into the circular economy has increased collaboration between the public sector, academia, and industry. Furthermore, comprehensive cost-benefit analyses (CBA) and LCA may support the implementation of the suggested technologies as workable substitutes. Moreover, valorisation procedures are more dependable as compared to conventional disposal methods because they generate value and minimise pollution, even when the market value of the recovered materials may not be high enough to justify their application.</p>
</sec>
</body>
<back>
<sec id="s8">
<title>Author contributions</title>
<p>SK compiled and edited the manuscript. SS and RY framed the concept and worked on the figures and tables. AS supervised the various concepts distributed across the institutions. AM completed the final editing. All authors contributed to the article and approved the submitted version.</p>
</sec>
<sec id="s9">
<title>Funding</title>
<p>The authors gratefully acknowledge the reviewers for their insightful comments and suggestions. SS acknowledges financial assistance in the form of a research project under Women Scientist Scheme-B, WISE-KIRAN DIVISION, Department of Science and Technology, Ministry of Science and Technology, Government of India (Project Grant No. DST/WOS-B/2018/1589).</p>
</sec>
<sec sec-type="COI-statement" id="s10">
<title>Conflict of interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="disclaimer" id="s11">
<title>Publisher&#x2019;s note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
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