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Topic Editors

Chemical & Materials Engineering Department, University of Cincinnati, Cincinnati, OH 45221, USA
Water Science PL and Alluvium Consulting Australia, Monash University, Echuca, Australia

Sustainable Technologies for Water Purification

Abstract submission deadline
30 September 2025
Manuscript submission deadline
30 November 2025
Viewed by
11098

Topic Information

Dear Colleagues,

A large amount of emerging environmental contaminants, such as antibiotics, organic dyes, pesticides, heavy metal ions, and so on, are emitted daily into water bodies due to industrialization, which leads to a worsening crisis for water environments. Water scarcity has resulted in severe challenges. A variety of emerging technologies concerning water purification and treatment, such as membrane filtration, adsorption, chemical oxidation, catalytic degradation, biotechnology, and so on, have been developed to decrease pollution efficiently. This Special Issue “Sustainable Technologies for Water Purification” discusses relevant sustainable technologies for water and wastewater treatment pertaining to a nanoscale approach, membrane-based technologies for water recovery and reuse, the energy and water nexus, degradation of organic pollutants, nascent technologies, bio and bio-inspired materials for water reclamation and integrated systems, and an overview of wastewater treatment plants.

Prof. Dr. Rakesh Govind
Dr. Barry T. Hart
Topic Editors

Keywords

  • wastewater treatment
  • water treatment
  • environmental biotechnology
  • water quality
  • bioremediation
  • membranes
  • biodegradation

Participating Journals

Journal Name Impact Factor CiteScore Launched Year First Decision (median) APC
Molecules
molecules
4.2 7.4 1996 15.1 Days CHF 2700 Submit
Pollutants
pollutants
- - 2021 25.3 Days CHF 1000 Submit
Separations
separations
2.5 3.0 2014 15.1 Days CHF 2600 Submit
Sustainability
sustainability
3.3 6.8 2009 19.7 Days CHF 2400 Submit
Water
water
3.0 5.8 2009 17.5 Days CHF 2600 Submit

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Published Papers (6 papers)

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37 pages, 10373 KiB  
Article
A Sustainable Approach in the Removal of Pharmaceuticals: The Effects of Operational Parameters in the Photocatalytic Degradation of Tetracycline with MXene/ZnO Photocatalysts
by Zeynep Karcıoğlu Karakaş and Zeliha Dönmez
Sustainability 2025, 17(5), 1904; https://doi.org/10.3390/su17051904 - 24 Feb 2025
Viewed by 216
Abstract
Zinc oxide (ZnO) is a vital semiconductor that is widely used for a wide variety of purposes. It is known that this material has a wide bandgap, and this property makes it sensitive to UV radiation. This way, ZnO nanoparticles can be used [...] Read more.
Zinc oxide (ZnO) is a vital semiconductor that is widely used for a wide variety of purposes. It is known that this material has a wide bandgap, and this property makes it sensitive to UV radiation. This way, ZnO nanoparticles can be used as photocatalysts in various processes and exhibit excellent catalytic activity. This study aims to produce a new and effective catalyst by combining ZnO nanoparticles used as photocatalysts with MXene, a two-dimensional material. MXenes have a great potential in terms of environmental sustainability. MXenes offer a wide range of sustainable solutions, from energy storage to water treatment, carbon capture to environmentally friendly electronics. The studies carried out for this purpose were carried out in two stages. In the first part, the composite particle was synthesized. In the second part, the produced composite was used as a photocatalyst in the photocatalytic degradation of tetracycline, an endocrine disruptor commonly encountered in wastewater. Optimum conditions were determined for operational parameters such as catalyst dosage, pollutant concentration, pH, irradiation time, light intensity, and temperature, which have the potential to affect the process efficiency significantly. The experiments conducted under optimum conditions determined that the organic pollutant in the solution was removed entirely. Full article
(This article belongs to the Topic Sustainable Technologies for Water Purification)
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Figure 1
<p>The schematic representation of the synthesis process designed for the synthesis of MXene@ZnO composite.</p>
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<p>A schematic representation of the experimental setup to be used for photocatalysis experiments.</p>
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<p>X-ray diffractograms of synthesized products and MAX phase, (<b>a</b>) MAX Phase, (<b>b</b>) MXene, (<b>c</b>) Standard diffraction pattern for ZnO, (<b>d</b>) ZnO nanoparticle, (<b>e</b>) MXene/ZnO nanocomposite.</p>
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<p>SEM images of MAX phase and synthesized MXene and ZnO (<b>a</b>,<b>b</b>) MAX phase; (<b>c</b>,<b>d</b>) MXene; (<b>e</b>,<b>f</b>) ZnO.</p>
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<p>SEM images of MXene/ZnO sample (<b>a</b>,<b>b</b>) SEM images; (<b>c</b>) particle-size-distribution histogram.</p>
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<p>SEM-EDX spectra were obtained for the MAX phase sample and the synthesized MXene, ZnO, and MXene/ZnO samples.</p>
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<p>TEM images of synthesized MXene/ZnO photocatalyst.</p>
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<p>Adsorption–desorption isotherms of synthesized samples (<b>a</b>) MXene, (<b>b</b>) MXene/ZnO.</p>
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<p>Data obtained from experiments to examine the effect of irradiation time: (<b>a</b>) changes in the concentration ratio; (<b>b</b>) compatibility with the kinetic model.</p>
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<p>A schematic representation of the possible mechanism for the photocatalytic activities of MXene/ZnO composites.</p>
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<p>Zeta potential (mV) values measured in the pH 2–12 range for MXene/ZnO photocatalyst.</p>
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<p>Data obtained from experiments to examine the effect of the initial pH value: (<b>a</b>) changes in the concentration ratio; (<b>b</b>) compatibility with the kinetic model.</p>
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<p>Relationship between initial pH values and final removal efficiencies.</p>
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<p>Data obtained from experiments to examine the effect of the catalyst dosage: (<b>a</b>) changes in the concentration ratio; (<b>b</b>) compatibility with the kinetic model.</p>
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<p>Data obtained from experiments to examine the effect of the temperature: (<b>a</b>) changes in the concentration ratio; (<b>b</b>) compatibility with the kinetic model.</p>
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<p>Data obtained from experiments to examine the effect of the initial pollutant concentration: (<b>a</b>) changes in the concentration ratio; (<b>b</b>) compatibility with the kinetic model.</p>
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<p>Data obtained from experiments to examine the effect of the light intensity: (<b>a</b>) changes in the concentration ratio; (<b>b</b>) compatibility with the kinetic model.</p>
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<p>Data obtained from experiment conducted under optimum conditions: (<b>a</b>) changes in the concentration ratio; (<b>b</b>) compatibility with the kinetic model.</p>
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<p>Experimental data obtained from reusability experiments conducted in cycles for MXene/ZnO photocatalyst.</p>
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37 pages, 11182 KiB  
Article
Conventional and Emerging Desalination Technologies: Review and Comparative Study from a Sustainability Perspective
by Jamel Orfi, Raed Sherif and Musaad AlFaleh
Water 2025, 17(2), 279; https://doi.org/10.3390/w17020279 - 20 Jan 2025
Viewed by 1730
Abstract
This work develops a comprehensive review of the main conventional and emerging desalination processes. It presents the state of knowledge of the most known and investigated techniques, highlights their advantages and drawbacks, and draws appropriate conclusions on their respective performances from various angles [...] Read more.
This work develops a comprehensive review of the main conventional and emerging desalination processes. It presents the state of knowledge of the most known and investigated techniques, highlights their advantages and drawbacks, and draws appropriate conclusions on their respective performances from various angles including their energy consumption and efficiency, environmental impacts, reliability, and flexibility in operations. This review reveals the recent large dominance and deployment of the reverse osmosis technology in the Gulf countries, mainly in Saudi Arabia; the importance of hybridization; and the slow penetration of promising processes including membrane distillation and forward osmosis into the industrial desalination market. In addition, this work aims to develop some comparison exercises between these processes using specific criteria. A cross approach allowing an easier comparison between various desalination processes could help identify the advantages and drawbacks of each technology and select the appropriate process. Therefore, various criteria allowing a clear picture to be drawn of the performance and capabilities of the main conventional and emerging desalination processes have been proposed in the frame of sustainable development. As an illustration of this general approach from sustainability prospects and considering specific weights for each proposed criterion for the case of Saudi Arabia, a comparison exercise reveals that the superiority of reverse osmosis (RO) is confirmed. Multiple effect distillation (MED) and membrane distillation (MD) processes are potentially competitive to RO while multi-stage flash (MSF) comes last due to several drawbacks. Full article
(This article belongs to the Topic Sustainable Technologies for Water Purification)
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<p>Contracted seawater/brackish water desalination capacity in the GCC countries [<a href="#B1-water-17-00279" class="html-bibr">1</a>].</p>
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<p>Overall picture of the Saudi seawater desalination plants and capacities (the numbers x/y refer to the number of plants in the region and the corresponding total daily capacity in m<sup>3</sup>, respectively), (adapted from [<a href="#B2-water-17-00279" class="html-bibr">2</a>]).</p>
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<p>Ways of classifying desalination processes.</p>
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<p>Schematic diagram of a parallel feed configuration MED unit with 5 effects.</p>
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<p>Schematic diagram of a parallel cross MED with preheaters and a TVC system [<a href="#B9-water-17-00279" class="html-bibr">9</a>].</p>
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<p>A schematic diagram of a once-through MSF plant.</p>
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<p>A schematic diagram of an MSF structure with brine recirculation [<a href="#B9-water-17-00279" class="html-bibr">9</a>].</p>
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<p>Schematic diagrams of (<b>A</b>) mechanical vapor compression and (<b>B</b>) thermo-vapor compression desalination [<a href="#B9-water-17-00279" class="html-bibr">9</a>].</p>
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<p>Schematic diagrams of (<b>A</b>) mechanical vapor compression and (<b>B</b>) thermo-vapor compression desalination [<a href="#B9-water-17-00279" class="html-bibr">9</a>].</p>
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<p>Reverse osmosis as a filtration system [<a href="#B48-water-17-00279" class="html-bibr">48</a>].</p>
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<p>Illustration of a typical SWRO desalination plant showing its main components (BP: Booster pump; HPP: high-pressure pump; ERD: Energy recovery device) [<a href="#B49-water-17-00279" class="html-bibr">49</a>].</p>
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<p>Permeate water crossing the pores of a semi-permeable membrane in a spiral-wound configuration [<a href="#B50-water-17-00279" class="html-bibr">50</a>].</p>
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<p>A simplified diagram illustrating the principle of the electrodialysis desalination process (adapted from [<a href="#B60-water-17-00279" class="html-bibr">60</a>]).</p>
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<p>A schematic of the humidification-dehumidification (HDH) process [<a href="#B61-water-17-00279" class="html-bibr">61</a>].</p>
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<p>Main components of freezing desalination (FD): pre-cooler, crystallizer, and melting unit [<a href="#B62-water-17-00279" class="html-bibr">62</a>].</p>
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<p>Schematic diagram of a capacitive deionization (CDI) process (adapted from [<a href="#B64-water-17-00279" class="html-bibr">64</a>]).</p>
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<p>(<b>a</b>) Basic distillation system and (<b>b</b>) Membrane distillation system [<a href="#B71-water-17-00279" class="html-bibr">71</a>].</p>
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<p>Main ways to improve the performance of membrane distillation systems.</p>
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<p>Basic MD configurations: (<b>a</b>) Direct contact membrane distillation (DCMD), (<b>b</b>) Air gap membrane distillation (AGMD), (<b>c</b>) sweeping gas membrane distillation (SGMD), and (<b>d</b>) Vacuum membrane distillation (VMD) [<a href="#B74-water-17-00279" class="html-bibr">74</a>].</p>
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<p>MD modules: <b>left</b>—plate-frame, and <b>right</b>—spiral-wound [<a href="#B74-water-17-00279" class="html-bibr">74</a>].</p>
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<p>Performance illustration of pilot scale MD variants expressed as gain output ratio (GOR) and transmembrane flux [<a href="#B16-water-17-00279" class="html-bibr">16</a>]. (AGMD: air gap membrane distillation; V-AGMD: vacuum-enhanced AGMD; and PGMD: permeate gap membrane distillation).</p>
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<p>Principle and main sub-systems of an FO unit.</p>
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<p>A schematic of the FO principle and the need to include a step of draw regeneration in the process [<a href="#B77-water-17-00279" class="html-bibr">77</a>].</p>
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<p>Schematic diagram of (<b>a</b>) the FO membrane process and (<b>b</b>) the MD process for desalination [<a href="#B79-water-17-00279" class="html-bibr">79</a>].</p>
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<p>Annual profit for several desalination processes in individual or MD hybrid configurations (TMD refers to MD) [<a href="#B83-water-17-00279" class="html-bibr">83</a>].</p>
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<p>Basic benefit of integrating AD with MED [<a href="#B86-water-17-00279" class="html-bibr">86</a>].</p>
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<p>Increase in water production due to the integration of AD and MED units [<a href="#B86-water-17-00279" class="html-bibr">86</a>].</p>
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<p>Overview of the renewable energy-desalination integrated processes worldwide (Ahmadi et al. [<a href="#B92-water-17-00279" class="html-bibr">92</a>]).</p>
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<p>Comparison of standalone and hybrid membrane-based systems (Skuse et al. [<a href="#B50-water-17-00279" class="html-bibr">50</a>]).</p>
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<p>Proposed metrics for comparison of main conventional and emerging desalination processes.</p>
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21 pages, 1613 KiB  
Article
Targets for Urban Stormwater Management in Australia
by Dan O’Halloran, Jonathon McLean, Peter Morison, Alex Sims, Tony Weber, Kim Markwell, Ben Walker, Oliver Light and Barry Hart
Water 2024, 16(24), 3686; https://doi.org/10.3390/w16243686 - 20 Dec 2024
Viewed by 700
Abstract
Increasing urbanisation is occurring in Australia’s major cities and in almost every country in the world. This creates a challenge for the urban water sector, which not only needs to provide traditional water services (i.e., wastewater, domestic water) for a rapidly growing population, [...] Read more.
Increasing urbanisation is occurring in Australia’s major cities and in almost every country in the world. This creates a challenge for the urban water sector, which not only needs to provide traditional water services (i.e., wastewater, domestic water) for a rapidly growing population, but also to service potential additional demands to contribute to enhanced amenity, and to do so in the context of climate change. This paper is focused on stormwater management controls for the develop of new greenfield urban sites in the three major east coast Australian cities—Melbourne, Sydney and Brisbane. While stormwater management in all three cities is focused on the protection of community values of the waterways, including environment (ecology), amenity and recreation, the scale or type of the waterways considered is considerably different—Melbourne has adopted a regional waterway strategy, while the Sydney and Brisbane approach is more localised. Pollution load reduction targets (TSS, TP, TN and litter) from new urban areas have been enforced in all three cities for many years, although there is concern that these targets primarily aimed at protecting the values of downstream bays (e.g., Port Phillip Bay, Sydney Harbour and Morton Bay) will not necessarily protect the values of the contributing waterways. However, targets to control stormwater volumes entering waterways are proving to be considerably more difficult to both develop and implement. These targets are typically expressed as volumes of stormwater to be harvested and/or infiltrated for every additional hectare of directly connected impervious (DCI) surface created as a result of urban development. The three cities have approached the setting of stormwater flow targets somewhat differently, as is apparent from the details provided in the paper. Additionally, we argue that there is a need for the development of new targets related to the reuse of stormwater and its integration with wastewater and domestic water management. Full article
(This article belongs to the Topic Sustainable Technologies for Water Purification)
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<p>Map of Greater Melbourne showing the major waterways and the location of the Sunbury regional stormwater harvesting scheme.</p>
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<p>Diagram showing the nine key waterway values identified in the Greater Melbourne Healthy Waterways Strategy.</p>
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<p>Map of Greater Sydney showing the major waterways and the location of the Wianamatta–South Creek catchment.</p>
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<p>Map of South East Queensland showing the major waterways and the local government boundaries.</p>
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60 pages, 6757 KiB  
Review
Recent Advances in Ball-Milled Materials and Their Applications for Adsorptive Removal of Aqueous Pollutants
by Pei Gao, Xuanhao Fan, Da Sun, Guoming Zeng, Quanfeng Wang and Qihui Wang
Water 2024, 16(12), 1639; https://doi.org/10.3390/w16121639 - 7 Jun 2024
Cited by 2 | Viewed by 2929
Abstract
Ball milling, as a cost-effective and eco-friendly approach, has been popular in materials synthesis to solve problems involving toxic reagents, high temperatures, or high pressure, which has the potential for large-scale production. However, there are few reviews specifically concentrating on the latest progress [...] Read more.
Ball milling, as a cost-effective and eco-friendly approach, has been popular in materials synthesis to solve problems involving toxic reagents, high temperatures, or high pressure, which has the potential for large-scale production. However, there are few reviews specifically concentrating on the latest progress in materials characteristics before and after ball milling as well as the adsorptive application for aqueous pollutants. Hence, this paper summarized the principle and classification of ball milling and reviewed the advances of mechanochemical materials in categories as well as their adsorption performance of organic and inorganic pollutants. Ball milling has the capacity to change materials’ crystal structure, specific surface areas, pore volumes, and particle sizes and even promote grafting reactions to obtain functional groups to surfaces. This improved the adsorption amount, changed the equilibrium time, and strengthened the adsorption force for contaminants. Most studies showed that the Langmuir model and pseudo-second-order model fitted experimental data well. The regeneration methods include ball milling and thermal and solvent methods. The potential future developments in this field were also proposed. This work tries to review the latest advances in ball-milled materials and their application for pollutant adsorption and provides a comprehensive understanding of the physicochemical properties of materials before and after ball milling, as well as their effects on pollutants’ adsorption behavior. This is conducive to laying a foundation for further research on water decontamination by ball-milled materials. Full article
(This article belongs to the Topic Sustainable Technologies for Water Purification)
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Figure 1
<p>Horizontal section of a grinding container and powder mixture [<a href="#B70-water-16-01639" class="html-bibr">70</a>]. Reprinted from Current Research Green and Sustainable Chemistry, 5, Thambiliyagodage C., Wijesekera R., Ball milling—A green and sustainable technique for the preparation of titanium based materials from ilmenite, 100236, Copyright (2022), with permission from Elsevier.</p>
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<p>The classification of ball mills: (<b>a</b>) a stirred ball mill, (<b>b</b>) a vibration ball mill, (<b>c</b>) a tumbler ball mill, and (<b>d</b>) a planetary ball mill [<a href="#B39-water-16-01639" class="html-bibr">39</a>,<a href="#B71-water-16-01639" class="html-bibr">71</a>]. Reprinted from Science of The Total Environment, 825, Yin Z., Zhang Q., Li S.; Cagnetta G., Huang J., Deng S., Yu G., Mechanochemical synthesis of catalysts and reagents for water decontamination: Recent advances and perspective, 153992, Copyright (2022), with permission from Elsevier. Reprinted from LET Electric Power Applications, 16, Xu Y., Zhang B., Feng G., Electromagnetic design and thermal analysis of module combined permanent magnet motor with wrapped type for mine ball mill, 139–157, Copyright (2021), with permission from Wiley.</p>
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<p>Schematic representation of (<b>a</b>) carboxylic groups-modified ACs (AC-COOH) [<a href="#B77-water-16-01639" class="html-bibr">77</a>], (<b>b</b>) ball-milled iron–biochar composites [<a href="#B79-water-16-01639" class="html-bibr">79</a>], (<b>c</b>) nanobiochars [<a href="#B80-water-16-01639" class="html-bibr">80</a>], (<b>d</b>) thiol-modified biochars [<a href="#B55-water-16-01639" class="html-bibr">55</a>], (<b>e</b>) BM-FeS@NBCs [<a href="#B10-water-16-01639" class="html-bibr">10</a>] preparation. (<b>a</b>) Reprinted from Journal of Molecular Liquids, 346, Sh. Gohr M., Abd-Elhamid A.I., El-Shanshory A.A., Soliman H.M.A., Adsorption of cationic dyes onto chemically modified activated carbon: Kinetics and thermodynamic study, 118227, Copyright (2022), with permission from Elsevier. (<b>b</b>) Reprinted from Environmental Science And Pollution Research, 30, Chen C., Yang F., Beesley L., Trakal L., Ma Y., Sun Y., Zhang Z., Ding Y., Removal of cadmium in aqueous solutions using a ball milling-assisted one-pot pyrolyzed iron-biochar composite derived from cotton husk, 12571–12583, Copyright (2023), with permission from Springer Nature. (<b>c</b>) Reprinted from Journal of Cleaner Production, 164, Naghdi M., Taheran M., Brar S.K., Rouissi T., Verma M., Surampalli R.Y., Valero J.R., A green method for production of nanobiochar by ball milling-optimization and characterization, 1394–1405, Copyright (2017), with permission from Elsevier. (<b>d</b>) Reprinted from Chemosphere, 294, Zhao L., Zhang Y., Wang L., Lyu H., Xia S., Tang J., Effective removal of Hg(ΙΙ) and MeHg from aqueous environment by ball milling aided thiol-modification of biochars: Effect of different pyrolysis temperatures, 133820., Copyright (2022), with permission from Elsevier. (<b>e</b>) Reprinted from Environmental Pollution, 306, Qu J., Zhang W., Bi F., Yan S., Miao X., Zhang B., Wang Y., Ge C., Zhang Y., Two-step ball milling-assisted synthesis of N-doped biochar loaded with ferrous sulfide for enhanced adsorptive removal of Cr(VI) and tetracycline from water, 119398, Copyright (2022), with permission from Elsevier.</p>
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<p>Schematic diagram of (<b>a</b>) FeOx@CNTs [<a href="#B66-water-16-01639" class="html-bibr">66</a>] and (<b>b</b>) PGO preparation [<a href="#B121-water-16-01639" class="html-bibr">121</a>]. (<b>a</b>) Reprinted from Chemosphere, 288, Cheng Z., Lyu H., Shen B., Tian J., Sun Y., Wu C., Removal of antimonite (Sb(III)) from aqueous solution using a magnetic iron-modified carbon nanotubes (CNTs) composite: Experimental observations and governing mechanisms, 132581, Copyright (2022), with permission from Elsevier. (<b>b</b>) Reprinted from Nanomaterials, 9, Olszewski R., Nadolska M., Lapinski M., Przesniak-Welenc M., Cieslik B.M., Zelechowska K., Solvent-free synthesis of phosphonic graphene derivative and its application in mercury ions adsorption, 485, Copyright (2019), with permission from MDPI.</p>
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<p>Mechanochemical synthesis of ZVIs [<a href="#B144-water-16-01639" class="html-bibr">144</a>]. Reprinted from Journal of Environment Management, 181, Ambika S., Devasena M., Nambi I.M., Synthesis, characterization and performance of high energy ball milled meso-scale zero valent iron in Fenton reaction, 847–855, Copyright (2016), with permission from Elsevier.</p>
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<p>Mechanism diagrams of governing mechanisms of (<b>a</b>) Ni(II) adsorption onto unmilled and milled biochars [<a href="#B86-water-16-01639" class="html-bibr">86</a>]; (<b>b</b>) Cd(II), Cu(II), and Pb(II) adsorption on BM-NBBCs [<a href="#B169-water-16-01639" class="html-bibr">169</a>]; (<b>c</b>) U(VI) uptake on PFBCs [<a href="#B89-water-16-01639" class="html-bibr">89</a>]. (<b>a</b>) Reprinted from Environmental Pollution, 233, Lyu H., Gao B., He F.; Zimmerman A.R., Ding C., Huang H., Tang J., Effects of ball milling on the physicochemical and sorptive properties of biochar: Experimental observations and governing mechanisms, 54–63, Copyright (2018), with permission from Elsevier. (<b>b</b>) Reprinted from Journal of Hazardous Materials, 387, Xiao J.; Hu R.; Chen G., Micro-nano-engineered nitrogenous bone biochar developed with a ball-milling technique for high-efficiency removal of aquatic Cd(II), Cu(II) and Pb(II), 121980, Copyright (2020), with permission from Elsevier. (<b>c</b>) Reprinted from Journal of Molecular Liquids, 303, Zhou Y., Xiao J., Hu R., Wang T., Shao X., Chen G., Chen L., Tian X., Engineered phosphorous-functionalized biochar with enhanced porosity using phytic acid-assisted ball milling for efficient and selective uptake of aquatic uranium, 112659, Copyright (2020), with permission from Elsevier.</p>
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<p>Mechanism diagrams of governing mechanisms of MB adsorption onto unmilled and milled biochars [<a href="#B181-water-16-01639" class="html-bibr">181</a>]. Reprinted from Chemical Engineering Journal, 335, Lyu H., Gao B., He F., Zimmerman A.R., Ding C., Tang J., Crittenden J.C. Experimental and modeling investigations of ball-milled biochar for the removal of aqueous methylene blue, 110–119, Copyright (2018), with permission from Elsevier.</p>
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15 pages, 6185 KiB  
Article
The Molecular Identification and Comprehensive Analysis of Klebsiella pneumoniae Isolated from Industrial Wastewater
by Kai Yan, Changfu Li, Weiyu Wang, Juan Guo and Haifeng Wang
Separations 2024, 11(4), 121; https://doi.org/10.3390/separations11040121 - 17 Apr 2024
Viewed by 2262
Abstract
Industrial wastewater typically contains many organic and inorganic pollutants and is also contaminated by various microorganisms. Microbial species in industrial wastewater have not been extensively investigated. In this experiment, a Klebsiella pneumoniae strain was isolated for the first time from industrial wastewater containing [...] Read more.
Industrial wastewater typically contains many organic and inorganic pollutants and is also contaminated by various microorganisms. Microbial species in industrial wastewater have not been extensively investigated. In this experiment, a Klebsiella pneumoniae strain was isolated for the first time from industrial wastewater containing a high concentration of sulfate and phosphate. Mass spectrometry, genetic analysis, and biochemical identification were conducted to understand the genetic and biochemical characteristics of this Klebsiella pneumoniae strain recovered from industrial wastewater. Growth experiments revealed that it exhibited an excellent growth rate in nutrient broth. Further analyses showed that the strain was sensitive to most antibiotics but resistant to chloramphenicol and nitrofurantoin. It also exhibited significant resistance to piperacillin/tazobactam and cefotaxime/clavulanic acid. Resistance gene experiments indicated the presence of gyrA, OqxB, and ParC genes associated with antibiotic resistance in the isolated Klebsiella pneumoniae strain. Proteomics uncovered the following three proteins related to drug resistance: the multi-drug resistant outer membrane protein MdtQ, the multi-drug resistant secretion protein, and the modulator of drug activity B, which are coexistent in Klebsiella pneumoniae. Proteomics and bioinformatics analyses further analyzed the protein composition and functional enrichment of Klebsiella pneumoniae. The isolation of Klebsiella pneumoniae from a high concentration in sulfate and phosphate industrial wastewater provides a new direction for further research on the characteristics and drug resistance traits of industrial wastewater microorganisms and the potential risks they may pose when released into the environment. Full article
(This article belongs to the Topic Sustainable Technologies for Water Purification)
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<p>MALDI-TOF MS identification of the isolated <span class="html-italic">Klebsiella pneumoniae</span> strain at different growth times and phylogenetic tree analysis. (<b>A</b>–<b>D</b>) represents the MALDI-TOF MS identification results of colony samples cultured for 12, 16, 20, and 24 h. (<b>E</b>) represents the phylogenetic tree based on 16S rDNA gene sequences.</p>
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<p>Growth curve of the isolated <span class="html-italic">Klebsiella pneumoniae</span> strain. After 90 h of culture, the growth characteristics of <span class="html-italic">Klebsiella pneumoniae</span> at different inoculum sizes were evaluated. (<b>A</b>) represents the control without inoculation (blank control), while (<b>B</b>–<b>H</b>) represents the growth of <span class="html-italic">Klebsiella pneumoniae</span> with different inoculum sizes.</p>
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<p>Analysis of drug resistance genes in <span class="html-italic">Klebsiella pneumoniae</span> isolated from industrial wastewater. The bacterial genomic and plasmid DNA were used as templates for amplification with specific primers, and then the electrophoresis bands were sequenced. (<b>A</b>–<b>I</b>) represent the nucleic acid gel images of drug-resistance genes.</p>
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<p>Analysis of drug resistance genes in <span class="html-italic">Klebsiella pneumoniae</span> isolated from industrial wastewater. The bacterial genome and plasmids were used as templates for amplification with specific primers, and then the electrophoresis bands were sequenced. (<b>A</b>–<b>I</b>) represent the nucleic acid gel images of drug-resistance genes.</p>
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<p>GO classification of proteomics data for <span class="html-italic">Klebsiella pneumoniae</span>. (<b>A</b>), BP dotplot; (<b>B</b>), CE dotplot; (<b>C</b>), dotplot; (<b>D</b>), the x-axis represents protein count, and the y-axis represents GO term name.</p>
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<p>KEGG pathways of proteomics data for <span class="html-italic">Klebsiella pneumoniae</span>. (<b>A</b>), KEGG dot plot; (<b>B</b>), KEGG fisher barplot; (<b>C</b>), level 1 represents the classification of environmental information processing, genetic information processing, and metabolism; and level 2 represents the classification of metabolic and functional pathways.</p>
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18 pages, 4314 KiB  
Article
The Application of an Electrocoagulation Process to the Sustainable Treatment of Initial Rainwater and the Simulation of a Flow Pattern in an Experimental Device
by Haiyan Yang, Zhe Wang, Kai Fu and Qingda Luo
Sustainability 2024, 16(1), 161; https://doi.org/10.3390/su16010161 - 23 Dec 2023
Viewed by 1478
Abstract
The pollutant content in initial rainwater is very high, so the treatment and research of initial rainwater has become an engagement issue in controlling non-point source pollution and realizing sustainable development in Chinese cities. This study explores the best flow pattern suitable for [...] Read more.
The pollutant content in initial rainwater is very high, so the treatment and research of initial rainwater has become an engagement issue in controlling non-point source pollution and realizing sustainable development in Chinese cities. This study explores the best flow pattern suitable for treating initial rainwater by electrocoagulation (EC), and a pilot-scale experiment is conducted to analyze the effect of the EC process on the treatment of initial rainwater. The findings indicate that the latter enhances the turbulent flow effect and the EC process treatment effect better under the two flow modes of parallel perforation flow and dislocation perforation flow. For the dislocation perforated flow pattern, the removal rates of suspended matter (SS), chemical oxygen demand (COD), and phosphorus (TP) are 94.00%, 81.95%, and 98.97%, respectively, which reach the expected treatment targets. Using the electrocoagulation–filtration (ECF) process to treat initial rainwater, the final effluent exhibits high quality and could be used as urban circulating cooling water. Specifically, SS, COD, and TP concentrations are 15.00 mg/L, 21.06 mg/L, and 0.11 mg/L, respectively. The hydraulic retention time of the process is short, only 30 min, and the energy consumption is low, 0.57 kWh. This study provides a reference for the sustainable treatment of early urban rainwater and the design of the flow pattern of the EC process. Full article
(This article belongs to the Topic Sustainable Technologies for Water Purification)
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Figure 1

Figure 1
<p>Experimental device diagram. (<b>a</b>) Plan view of the EC device: 1. water intake tank; 2. water inlet pipe; 3. peristaltic pump; 4. electrocoagulation reactor; 5. perforated plate; 6. cathode power line; 7. DC power supply; 8. anode power line; 9. water outlet pipe; 10. sedimentation tank. (<b>b</b>) Plan view of the pilot-scale ECF reactor: 1. water inlet pipe; 2. lift pump; 3. EC device; 4. DC power supply; 5. cathode power cord; 6. anode power cable; 7. perforated plate; 8. slag baffle plate; 9. inclined plate sedimentation tank; 10. mud pipe; 11. discharge pipe of the electrocoagulation device; 12. filter basin; 13. overflow trough; 14. filter material layer; 15. aeration pipe; 16. filter outlet pipe. (<b>c</b>) Site layout of the EC device.</p>
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<p>The layout of the metal plate in the EC device and internal grid division diagram. (<b>a</b>) Parallel perforation; (<b>b</b>) dislocation perforation.</p>
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<p>A streamline diagram and kinetic energy diagram of the fluid in the device under different flow conditions. (<b>a</b>) Parallel perforated flow; (<b>b</b>) dislocation perforated flow.</p>
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<p>The removal effect of the EC device on each pollutant under different flow conditions. (<b>a</b>) Parallel perforated flow; (<b>b</b>) dislocation perforated flow.</p>
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<p>The removal effect of the EC process on pollutants. (<b>a</b>) The trial operation results of the pilot experiment under four working conditions; (<b>b</b>) the results of the continuous operation experiment of the pilot plant.</p>
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