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Clean Technol., Volume 6, Issue 4 (December 2024) – 18 articles

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24 pages, 1208 KiB  
Article
Enhancing Environmental Performance: A Method for Identifying and Prioritizing Key Environmental Issues in Industry
by Dellise Marie, Jonathan Villot, Rodolphe Gaucher, Anne Amardeil and Valérie Laforest
Clean Technol. 2024, 6(4), 1653-1676; https://doi.org/10.3390/cleantechnol6040080 - 13 Dec 2024
Viewed by 473
Abstract
BAT-based regulations necessitate defining key environmental issues (KEIs) to focus data collection and discussions on the main topics when establishing best available techniques (BATs) at the sector level. However, Article 14 of the Industrial Emissions Directive (IED) suggests that some significant environmental issues [...] Read more.
BAT-based regulations necessitate defining key environmental issues (KEIs) to focus data collection and discussions on the main topics when establishing best available techniques (BATs) at the sector level. However, Article 14 of the Industrial Emissions Directive (IED) suggests that some significant environmental issues may not be covered by BAT conclusions but still require the implementation of BATs at the local level, even in the absence of defined sectoral BAT references. The IED, along with the associated Commission Implementing Decisions and guides, does not offer guidelines for selecting KEIs at the local level, whether by the competent authority or the operator. To ensure full compliance with the IED by installations under its scope, this paper proposes a methodology for determining KEIs locally. Based on the environmental aspects of the installation, the sensitivity of the environment, and the levels of emissions or consumption, this methodology has been tested on a case study at the plant level to demonstrate its effectiveness. The paper then discusses the contributions and limitations of the methodology and suggests areas for future research. The proposed methodology was tested at the factory level, where it effectively identified and prioritized key environmental issues (KEIs) by focusing on site-specific environmental aspects not covered by sectoral BAT conclusions. The results suggested improved alignment with local environmental challenges, indicating the methodology’s effectiveness in capturing key issues that may require immediate action under Article 14 of the IED. This approach provides a practical framework for prioritizing environmental impacts based on local context and regulatory requirements. Full article
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<p>Synoptic of the preliminary determination of KEIs at the European level [<a href="#B17-cleantechnol-06-00080" class="html-bibr">17</a>].</p>
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<p>Main steps of the methodology.</p>
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<p>Selection procedure of KEIs. (<b>A</b>): equation for the assessment of the global score, (<b>B</b>): score scale.</p>
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28 pages, 3450 KiB  
Article
Harvesting Renewable Energy to Supply Power for Electric Buses
by Shwan Hussein Awla and Simon P. Philbin
Clean Technol. 2024, 6(4), 1625-1652; https://doi.org/10.3390/cleantechnol6040079 - 12 Dec 2024
Viewed by 604
Abstract
This research study addresses the challenges of extended charging times and limited ranges in electric vehicles by conducting a techno-economic analysis of integrating renewable energy technologies—solar modules, wind turbines, and piezoelectric materials—into double-decker electric buses in London, UK. Consequently, the empirical study evaluates [...] Read more.
This research study addresses the challenges of extended charging times and limited ranges in electric vehicles by conducting a techno-economic analysis of integrating renewable energy technologies—solar modules, wind turbines, and piezoelectric materials—into double-decker electric buses in London, UK. Consequently, the empirical study evaluates the power output of renewable energy technologies through simulation modelling based on vehicle specifications and energy requirements, which is followed by numerical modelling to assess economic viability. Furthermore, CFD (computational fluid dynamics) modelling is undertaken to examine the performance levels of vehicular-mounted wind turbines. The solar modules are placed on the rooftop and sides of the bus, generating 15.9 kWh/day, and the wind turbine in the front bumper of the bus generates 8.3 kWh/day. However, the piezoelectric material generated only 22.6 Wh/day, thereby rendering this technology impractical for further analysis. Therefore, both the solar modules and wind turbines combined generate 24.2 kWh/day, which can increase the driving range by 16.3 km per day, resulting in savings of 19.36 min for charging at the stations. Investing in such projects would have a positive return as the internal rate of return (IRR) and net present value (NPV) are 2.8% and £11,175, respectively. The annual revenue would be £6712, and the greenhouse gas (GHG) reduction would be two metric tons annually. Electricity generation, the electricity generation rate, and the initial investment are identified as key factors influencing power outages in a sensitivity analysis. In conclusion, this numerical modelling study paves the way for experimental validation toward the implementation of renewable energy technologies on electric bus fleets. Full article
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<p>Solar radiation vs. Total power generation [<a href="#B11-cleantechnol-06-00079" class="html-bibr">11</a>]. Solar radiation: the amount of energy emitted by the sun through electromagnetic form. Power generation: the process of generating electricity through energy conversion emitted from the sun.</p>
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<p>Comparison of increased cruising range of both photovoltaic (PV) and wind energy conversion systems (WECS) [<a href="#B22-cleantechnol-06-00079" class="html-bibr">22</a>].</p>
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<p>The main stages of analysis explaining theoretical modeling conducted for solar panels, mini-wind turbines, and piezo materials based on the power output of both NPV and IRR. This is calculated to determine the feasibility of such projects.</p>
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<p>Layout of the available area (highlighted in green) on the bus to install solar modules. The area highlighted in yellow is mostly used for advertising. White and Red areas are used for windows, doors, ventilation, and wind turbines [<a href="#B57-cleantechnol-06-00079" class="html-bibr">57</a>].</p>
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<p>CFD analysis of the bus for different speeds. Velocity streamlines around the bus show different effective wind speeds [<a href="#B63-cleantechnol-06-00079" class="html-bibr">63</a>].</p>
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<p>Power outage of Solar Modules (SM), Wind Turbine (WT), and Piezo Materials.</p>
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15 pages, 6822 KiB  
Article
Application of Carboxymethyl Cellulose (CMC)-Coated Nanoscale Zero-Valent Iron in Chromium-Containing Soil Remediation
by Bo Zhang, Jiani Zhan, Jiaqi Fan, Bohong Zhu, Weili Shen, Shiwei Zhang, Weiting Li, Zhaohui Li and Fanjun Zeng
Clean Technol. 2024, 6(4), 1610-1624; https://doi.org/10.3390/cleantechnol6040078 - 11 Dec 2024
Viewed by 607
Abstract
Nanofine zero−valent iron (nZVI) is a new, eco−friendly material with strong reducing and adsorbent properties that can be used to clean up heavy metal−affected soils. Herein, nZVI encapsulated with carboxymethyl cellulose (CMC−nZVI) is synthesized via an aqueous−phase reduction technique and subsequently deployed to [...] Read more.
Nanofine zero−valent iron (nZVI) is a new, eco−friendly material with strong reducing and adsorbent properties that can be used to clean up heavy metal−affected soils. Herein, nZVI encapsulated with carboxymethyl cellulose (CMC−nZVI) is synthesized via an aqueous−phase reduction technique and subsequently deployed to evaluate its effectiveness in Cr(VI) soil remediation. The characterization analysis used SEM−EDS, XRD, XPS, and LSV to determine the relevant properties of the material. The results show that at an initial Cr(VI) concentration of 169.5 mg·kg−1, 93.2% of Cr(VI) was removed from the soil after 10 h of treatment with CMC−nZVI at pH 3.3. The kinetic analysis showed that CMC−nZVI had the maximum equilibrium adsorption capacity for removing Cr(VI) from soil at 105.3 mg·g−1. This followed a pseudo−second−order kinetic model. The study shows that CMC−nZVI converts Cr(VI) to Cr(III), which forms complexes with Fe(III) ions in the presence of hydroxide ions (OH) to form a highly stable compound that eventually adsorbs into the nanomaterial’s surface for efficient removal. Full article
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<p>SEM images of (<b>a</b>) nZVI and (<b>b</b>) CMC−nZVI.</p>
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<p>XRD profiles of nZVI and CMC−nZVI.</p>
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<p>XPS pattern of (<b>a</b>) nZVI and (<b>b</b>) CMC−nZVI.</p>
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<p>LSV anodic polarization curves of nZVI and CMC−nZVI. (<b>b</b>) An enlarged view of the dashed box in (<b>a</b>).</p>
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<p>Images of antioxidant properties of different materials.</p>
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<p>(<b>a</b>) Pseudo−first−order kinetics model and (<b>b</b>) pseudo−second−order kinetics model.</p>
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<p>The adsorption isotherm of Cr (pH = 3.3, T = 25 °C) conforms to the Langmuir and Freundlich models.</p>
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<p>(<b>a</b>) SEM images of CMC−nZVI and (<b>b</b>) CMC−nZVI−Cr and (<b>c</b>,<b>d</b>) EDS images of CMC−nZVI−Cr. In (<b>d</b>), the blue color represents the C element, the red color represents the O element, the green color represents the Fe element, and the cyan color represents the Cr element.</p>
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<p>XRD images of CMC−nZVI and CMC−nZVI−Cr.</p>
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<p>E−pH diagram of the Cr−O<sub>2</sub>−H<sub>2</sub>O system.</p>
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<p>Removal mechanism for Cr(VI) by CMC−nZVI in soil.</p>
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16 pages, 2094 KiB  
Article
Energy Recovery from Cannabis Residues by Combustion with and Without Steam Explosion Pretreatment in Different Air Coefficients
by Rafael Eloy de Souza, Eduardo Lins de Barros Neto, Jean-Michel Lavoie and Bruna Rego de Vasconcelos
Clean Technol. 2024, 6(4), 1594-1609; https://doi.org/10.3390/cleantechnol6040077 - 2 Dec 2024
Viewed by 547
Abstract
Alternative options have been studied to mitigate the negative impact of fossil fuel sources, mainly especially when it comes to alternative energy sources. In this work, cannabis residues have been considered as a potential biomass residues for energy recovery due to their energy [...] Read more.
Alternative options have been studied to mitigate the negative impact of fossil fuel sources, mainly especially when it comes to alternative energy sources. In this work, cannabis residues have been considered as a potential biomass residues for energy recovery due to their energy content, and the increase in the cannabis market in Canada has created an opportunity niche for treating and valorizing these residues as energy. This study thus aims to investigate the potential of energy recovery from cannabis residue pellets via combustion and the impact of steam explosion on the pellets’ properties as well as combustion behavior. Two batches of pellets were produced namely with and without the steam explosion pretreatment. The properties of the pellets were then compared to those of the CANplus certification. Cannabis pellets were then combusted at 290 °C in a fixed-bed reactor using three different air coefficients (α) ranging from 1 to 1.3 (α = 1.0, α = 1.15, and α = 1.3). Flue gas quantification was performed using gas chromatography combined with a NOx detector. Results showed that the properties of this biomass is comparable to other sources of lignocellulosic biofuels. The steam explosion pretreatment enhanced pellet properties, including higher heating value (HHV), ash content, durability, and fines allowing the product to reach the CANplus requirements. The air coefficients influenced the emission levels, with an optimal value at α = 1.15, that indicated an improved combustion quality. However, steam explosion negatively affected combustion efficiency, resulting in incomplete combustion. Overall, cannabis residues show a strong potential for energy recovery and could offer a sustainable option for bioenergy applications. Full article
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<p>Overview of the experimental procedures used for pellet production, combustion as well as the analytical measurement performed on cannabis residues belonging to the strain “Powdered Donut). While the black square represents the unit operations performed on the biomass, the orange shows the analysis that were performed at each step.</p>
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<p>P&amp;ID of the semi-pilot fixed-bed set up for biomass combustion.</p>
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<p>Cannabis pellets produce from the “powdered donut” variety: (<b>a</b>) without steam explosion pretreatment and (<b>b</b>) with steam explosion pretreatment.</p>
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<p>TGA curves of cannabis pellets (“powdered donut” variety) under an air atmosphere at 20 °C/min: (<b>a</b>) without pretreatment and (<b>b</b>) pretreated by steam explosion.</p>
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<p>Influence of the air on gas emissions from the combustion of cannabis pellets (made from the residues of the “powdered donut” variety) without pretreatment at (<b>a</b>) α = 1.0, (<b>b</b>) α = 1.15, (<b>c</b>) α = 1.3 at 290 °C.</p>
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<p>Influence of the air on gas emissions from the combustion of cannabis pellets (made from the residues of the “powdered donut” variety) with a steam explosion pretreatment at (<b>a</b>) α = 1.0, (<b>b</b>) α = 1.15, (<b>c</b>) α = 1.3 at 290 °C.</p>
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15 pages, 8630 KiB  
Article
Carbon-Dioxide-Assisted Gasification of Sunflower Husk: An Impact of Iron, Nickel, or Cobalt Addition
by Artem A. Medvedev, Daria A. Beldova, Leonid M. Kustov, Mikhail Yu. Mashkin, Svetlana B. Polikarpova, Valentina Z. Dobrokhotova, Elena V. Murashova, Marina A. Tedeeva, Pavel V. Sokolovskiy and Alexander L. Kustov
Clean Technol. 2024, 6(4), 1579-1593; https://doi.org/10.3390/cleantechnol6040076 - 29 Nov 2024
Viewed by 359
Abstract
While the attempts to find new energy sources have intensified, the interest in the use of biomass as a carbon-rich raw material still is increasing. In this work, we studied iron-, cobalt-, and nickel-based materials in the process of CO2-assisted gasification [...] Read more.
While the attempts to find new energy sources have intensified, the interest in the use of biomass as a carbon-rich raw material still is increasing. In this work, we studied iron-, cobalt-, and nickel-based materials in the process of CO2-assisted gasification of sunflower husk. The materials with and without metal additives were examined by XRD, SEM, EDX, and TEM techniques and were tested in their gasification under the action of CO2. It was found that the Co-based material demonstrates the best activity among the studied ones (the CO2 conversion was up to 83%). The possible reason for such superiority may be related to the capability of Ni compounds to the formation of the metallic nickel phase and insufficient activity of iron species. Full article
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<p>SEM images of sunflower husk heated at 600 °C in a CO<sub>2</sub> flow.</p>
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<p>SEM images and element maps (Fe, Co, or Ni) for the samples before and after catalytic tests.</p>
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<p>SEM images and element maps (Fe, Co, or Ni) for the samples before and after catalytic tests.</p>
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<p>TEM image of the fresh pre-heated sunflower husk (the insertion) and energy-dispersion spectrum (the main picture).</p>
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<p>TEM image of the spent sunflower husk (the insertion) and energy-dispersion spectrum (the main picture).</p>
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<p>TEM images of the fresh catalytic materials heated at 600 °C for 1 h in a CO<sub>2</sub> stream.</p>
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<p>TEM images of the spent catalytic materials in CO<sub>2</sub>-assisted gasification of sunflower husk.</p>
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<p>Metal-containing particle distributions by size for the materials impregnated with 5 wt. % Fe, Co, or Ni, before and after the catalytic tests.</p>
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<p>XRD patterns of the samples after 600 °C heating in a CO<sub>2</sub> flow and the patterns of these samples after the gasification catalytic tests. The inset picture is the enlarged patten of the Ni-loaded sample.</p>
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<p>SAED patterns for the samples 5 Fe/SFH and 5 Ni/SFH, both fresh and spent. The sample 5 Co/SFH does not demonstrate any clear pattern (no rings shown here).</p>
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<p>SAED patterns for the samples 5 Fe/SFH and 5 Ni/SFH, both fresh and spent. The sample 5 Co/SFH does not demonstrate any clear pattern (no rings shown here).</p>
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<p>The results of the catalytic tests for the prepared metal-loaded materials and the starting sunflower husk in the reaction of CO<sub>2</sub>-assisted gasification at 800 °C.</p>
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<p>Yields of CO calculated on the basis of carbon dioxide converted for the prepared metal-loaded materials and the starting sunflower husk in the reaction of CO<sub>2</sub>-assisted gasification at 500–800 °C.</p>
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<p>An example of the component flows fitting. Green and red legends reflect to carbon dioxide and carbon monoxide components flows respectively. The blue legend reflects temperature in Celsius degree.</p>
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14 pages, 2776 KiB  
Article
Applying the Efficiency Analysis Tree Method for Enhanced Eco-Efficiency in Municipal Solid Waste Management: A Case Study of Chilean Municipalities
by Ramon Sala-Garrido, Manuel Mocholi-Arce, Maria Molinos-Senante and Alexandros Maziotis
Clean Technol. 2024, 6(4), 1565-1578; https://doi.org/10.3390/cleantechnol6040075 - 21 Nov 2024
Viewed by 486
Abstract
Enhancing the eco-efficiency of municipal solid waste (MSW) services is pivotal for the shift toward a circular economy. Although the Data Envelopment Analysis (DEA) method is widely used, it is susceptible to overfitting, potentially distorting eco-efficiency assessments. This study applies the efficiency analysis [...] Read more.
Enhancing the eco-efficiency of municipal solid waste (MSW) services is pivotal for the shift toward a circular economy. Although the Data Envelopment Analysis (DEA) method is widely used, it is susceptible to overfitting, potentially distorting eco-efficiency assessments. This study applies the efficiency analysis tree (EAT) method, which synergizes machine learning and linear programming, offering a more reliable framework for eco-efficiency evaluation in the MSW sector. This innovative approach provides deeper insights into the optimal levels of operational costs and unsorted waste. The research encompasses a case study of 98 Chilean municipalities from 2015 to 2019, uncovering significant disparities in optimal operational expenses and unsorted waste quantities, which underscores the necessity for customized waste management approaches. The average eco-efficiency scores for 2015–2019 range between 0.561 and 0.566. This means that assessed municipalities can reduce unsorted waste by amounts ranging from 1,632,409 tons/year (2016) to 1,822,663 tons/year (2018). Potential economic savings estimated are 105,973 USD/year (2019), which represents 44% of the total MSW management costs. Additionally, the investigation into the effects of external factors on eco-efficiency furnishes nuanced perspectives that can guide policymakers and municipal authorities in developing effective, context-specific waste management strategies. Beyond refining eco-efficiency evaluations, this study contributes to more informed decision-making processes, aiding the progression toward sustainable waste management practices. Full article
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<p>Efficiency analysis tree (EAT) for estimating optimal operational costs and unsorted waste, where Id denotes the node; n(t) shows the number of observations; y<sub>1</sub> is the maximum operating costs in USD per year; and y<sub>2</sub> is the maximum level of unsorted waste in tons per year.</p>
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<p>Statistics of eco-efficiency scores in the provision of municipal solid waste services for assessed municipalities.</p>
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<p>Potential reduction of unsorted waste expressed in tons per year and percentage in relation to total municipal solid waste generated.</p>
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<p>Potential economic savings in managing MSW expressed in USD per year and percentage in relation to total operational costs.</p>
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28 pages, 6565 KiB  
Article
Hybrid Electrocoagulation–Adsorption Process for Montelukast Sodium Removal from Water
by Sayedali Mirkhalafi, Khalid S. Hashim, Osamah Al-Hashimi and Ali Majdi
Clean Technol. 2024, 6(4), 1537-1564; https://doi.org/10.3390/cleantechnol6040074 - 20 Nov 2024
Viewed by 799
Abstract
This study addresses the significant environmental challenge of pharmaceutical pollutants by demonstrating the effectiveness of a hybrid electrocoagulation–adsorption (EC-A) technique for removing Montelukast Sodium (MS) from contaminated water. The research was conducted in three stages—adsorption, electrocoagulation, and adsorption using the residual water from [...] Read more.
This study addresses the significant environmental challenge of pharmaceutical pollutants by demonstrating the effectiveness of a hybrid electrocoagulation–adsorption (EC-A) technique for removing Montelukast Sodium (MS) from contaminated water. The research was conducted in three stages—adsorption, electrocoagulation, and adsorption using the residual water from the electrocoagulation process. The adsorbent materials were characterised using various analytical techniques: X-ray Diffraction (XRD) for determining the crystalline structure, Energy-Dispersive X-ray Spectroscopy (EDX) for elemental composition, Scanning Electron Microscopy (SEM) for surface morphology, and Fourier Transform Infrared Spectroscopy (FTIR) for identifying functional groups before and after interaction with the pollutants. The adsorption phase achieved optimal results at a pH of 3 and a contact time of 120 min, with a maximum removal efficiency of 99.5% for a starting MS concentration of 50 mg/L using Calcium Ferric Oxide–Silica Sand (CFO-SS) adsorbent. The electrocoagulation phase showed a 97% removal efficiency with a pH of 11, a current density of 20 mA, and a 5 mm electrode distance, achieved in just 20 min. Finally, the combined EC-A process, with the pH of residual water adjusted to 3, further enhanced the removal efficiency to 74%, highlighting the method’s potential for pharmaceutical contaminant removal. These findings underscore the potential of the EC-A technique as a highly effective and adaptable solution for mitigating pharmaceutical contaminants in water. Full article
(This article belongs to the Collection Water and Wastewater Treatment Technologies)
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<p>Montelukast Sodium (MS) chemical structure.</p>
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<p>Experimental setup for hybrid electrocoagulation–adsorption (EC-A) experiment.</p>
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<p>Calibration curve diagram and R<sup>2</sup> value for MS concentrations.</p>
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<p>Effect of adsorbent dosage on MS removal.</p>
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<p>Effect of pH on the performance of adsorbent on MS removal.</p>
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<p>Best removal efficiency of MS from water.</p>
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<p>Effect of pH on EC test in pH 3, 7, and 11 after 5, 10, 15, and 20 min of the test.</p>
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<p>Effect of distance between electrodes on the EC test with 5, 10, and 15 mm of electrode distances in pH 11, after 5, 10, 15, and 20 min of the test.</p>
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<p>Effect of current density on EC test in 10, 20, and 30 mA current, in pH 11 and 5 mm distance between electrodes after 5, 10, 15, and 20 min run.</p>
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<p>Effect of time on the best condition of EC test in pH 11, 5 mm of electrode distances, and 20 mA of current density after 10, 20, 30, 40, 50, and 60 min run.</p>
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<p>The removal efficiency of adsorption with EC residual water and the effect of adsorbent dosage on the removal in the best conditions (pH of 3, contact time of 120 min).</p>
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<p>The isotherm models’ rate constant using statistical data of MS sorption with activated sand.</p>
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<p>The XRD analysis for the activated sand.</p>
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<p>SEM pictures of raw sand (<b>a</b>), activated sand before interaction (<b>b</b>), activated sand after interaction with MS (<b>c</b>), and activated sand after interaction with the residual water after EC (<b>d</b>).</p>
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<p>EDX analysis for the raw sand (<b>a</b>), the sand after activation (<b>b</b>), and the comparison of chemicals present in the raw and activated sand (<b>c</b>).</p>
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<p>EDX analysis for the two samples after interaction with the pollutants: (<b>a</b>) activated sand after first adsorption batch test and (<b>b</b>) activated sand after the second adsorption batch test.</p>
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<p>FT-IR analysis for the raw sand (<b>a</b>), activated sand with ferric oxide (<b>b</b>), the sand after interaction with MS (<b>c</b>), and the sand after interaction with the residual water of EC treatment (<b>d</b>).</p>
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<p>FT-IR analysis for the raw sand (<b>a</b>), activated sand with ferric oxide (<b>b</b>), the sand after interaction with MS (<b>c</b>), and the sand after interaction with the residual water of EC treatment (<b>d</b>).</p>
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18 pages, 4284 KiB  
Article
Aeration Optimization for the Biodrying of Market Waste Using Negative Ventilation: A Lysimeter Study
by Ye Nyi Nyi Lwin, Abhisit Bhatsada, Sirintornthep Towprayoon, Suthum Patumsawad, Noppharit Sutthasil and Komsilp Wangyao
Clean Technol. 2024, 6(4), 1519-1536; https://doi.org/10.3390/cleantechnol6040073 - 20 Nov 2024
Viewed by 715
Abstract
This study investigates the optimization of aeration rates for the biodrying of market waste using negative-pressure ventilation. Market waste, characterized by a high moisture content (MC) and rapid decomposition, presents challenges in waste management. Over 12 days, three aeration rates (ARs) of 0.2, [...] Read more.
This study investigates the optimization of aeration rates for the biodrying of market waste using negative-pressure ventilation. Market waste, characterized by a high moisture content (MC) and rapid decomposition, presents challenges in waste management. Over 12 days, three aeration rates (ARs) of 0.2, 0.4, and 0.6 m3/kg/day were examined, and the most effective continuous ventilation configuration was identified in terms of heat generation, moisture reduction, and biodrying efficiency. The results indicate that the most effective AR for heat retention and moisture removal was 0.2 m3/kg/day, achieving a 6.63% MC reduction and a 9.12% low heating value (LHV) increase. Gas analysis showed that, while AR 0.2 supported high microbial activity during the initial 7 days, AR 0.6 sustained higher overall CO2 production due to its greater aeration rate. The findings also suggest that the biodrying of market waste with a high initial MC can achieve significant weight loss and leachate generation when paired with a high aeration rate of 0.6 m3/kg/day, with a 69.8% weight loss and increased waste compaction being recorded. The study suggests that variable ARs can optimize biodrying, making market waste more suitable for conversion to refuse-derived fuel or landfill pre-treatment and improving waste-to-energy processes and sustainability. Full article
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<p>Aerial view of waste sampling site at Praeksa Mai dumpsite and image showing typical characteristics of the studied market waste.</p>
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<p>Schematic of lysimeter design.</p>
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<p>Temperature evolution under different aeration rates: (<b>a</b>) AR 0.2, (<b>b</b>) AR 0.4, and (<b>c</b>) AR 0.6 (HP—heating phase, DP—declining phase, SP—stable phase).</p>
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<p>Plots showing the (<b>a</b>) temperature integration index and (<b>b</b>) temperature integration index by phase during biodrying (HP—heating phase, DP—declining phase, SP—stable phase).</p>
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<p>Observed CO<sub>2</sub> and O<sub>2</sub> concentrations during the biodrying process for (<b>a</b>) AR 0.2, (<b>b</b>) AR 0.4, and (<b>c</b>) AR 0.6; (<b>d</b>) average CO<sub>2</sub> generation in all three lysimeters.</p>
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<p>Plots showing physical changes throughout the experiment in (<b>a</b>) daily density and waste height and (<b>b</b>) weight loss and leachate production.</p>
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<p>Radar chart comparing the performance of different aeration rates.</p>
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<p>Schematic showing water balance calculation for the three studied lysimeters.</p>
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<p>Schematic showing the calculated carbon balance for the three lysimeters.</p>
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15 pages, 3772 KiB  
Article
The Recycling of Lithium from LiFePO4 Batteries into Li2CO3 and Its Use as a CO2 Absorber in Hydrogen Purification
by Zoltán Köntös and Ádám Gyöngyössy
Clean Technol. 2024, 6(4), 1504-1518; https://doi.org/10.3390/cleantechnol6040072 - 4 Nov 2024
Viewed by 1426
Abstract
The growing adoption of lithium iron phosphate (LiFePO4) batteries in electric vehicles (EVs) and renewable energy systems has intensified the need for sustainable management at the end of their life cycle. This study introduces an innovative method for recycling lithium from [...] Read more.
The growing adoption of lithium iron phosphate (LiFePO4) batteries in electric vehicles (EVs) and renewable energy systems has intensified the need for sustainable management at the end of their life cycle. This study introduces an innovative method for recycling lithium from spent LiFePO4 batteries and repurposing the recovered lithium carbonate (Li2CO3) as a carbon dioxide (CO2) absorber. The recycling process involves dismantling battery packs, separating active materials, and chemically treating the cathode to extract lithium ions, which produces Li2CO3. The efficiency of lithium recovery is influenced by factors such as leaching temperature, acid concentration, and reaction time. Once recovered, Li2CO3 can be utilized for CO2 capture in hydrogen purification processes, reacting with CO2 to form lithium bicarbonate (LiHCO3). This reaction, which is highly effective in aqueous solutions, can be applied in industrial settings to mitigate greenhouse gas emissions. The LiHCO3 can then be thermally decomposed to regenerate Li2CO3, creating a cyclic and sustainable use of the material. This dual-purpose process not only addresses the environmental impact of LiFePO4 battery disposal but also contributes to CO2 reduction, aligning with global climate goals. Utilizing recycled Li2CO3 decreases the demand for virgin lithium extraction, supporting a circular economy. Furthermore, integrating Li2CO3-based CO2 capture systems into existing industrial infrastructure provides a scalable and cost-effective solution for lowering carbon footprints while securing a continuous supply of lithium for future battery production. Future research should focus on optimizing lithium recovery methods, improving the efficiency of CO2 capture, and exploring synergies with other waste management and carbon capture technologies. This comprehensive strategy underscores the potential of lithium recycling to address both resource conservation and environmental protection challenges. Full article
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<p>Composition of a LiFePO<sub>4</sub> battery.</p>
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<p>The XRD spectra of the purified Li<sub>2</sub>CO<sub>3</sub>.</p>
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<p>The peek list and the identified components of the purified Li<sub>2</sub>CO<sub>3</sub>.</p>
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<p>Model of the CO<sub>2</sub> generator.</p>
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<p>Decomposition of Formic Acid.</p>
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<p>Model of the CO<sub>2</sub> absorber (gas separator).</p>
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<p>Reaction equlibra between Li<sub>2</sub>CO<sub>3</sub> and LiHCO<sub>3</sub>.</p>
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<p>Carbonate (red) and bicarbonate (green) concentrations in time.</p>
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<p>Identification of molecular hydrogen.</p>
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24 pages, 6433 KiB  
Article
Research on Hybrid Heating System in Cold Oilfield Regions
by Meng Xu, Zhiyang Xu, Xinxin Wei, Gaoxiang Zhang and Changyu Liu
Clean Technol. 2024, 6(4), 1480-1503; https://doi.org/10.3390/cleantechnol6040071 - 2 Nov 2024
Viewed by 812
Abstract
Efficient and clean treatment of wastewater and energy recovery and utilization are important links to realize low-carbon development of oilfields. Therefore, this paper innovatively proposes a multi-energy complementary co-production heating system which fully and efficiently utilizes solar energy resources, oilfield waste heat resources, [...] Read more.
Efficient and clean treatment of wastewater and energy recovery and utilization are important links to realize low-carbon development of oilfields. Therefore, this paper innovatively proposes a multi-energy complementary co-production heating system which fully and efficiently utilizes solar energy resources, oilfield waste heat resources, and biomass resources. At the same time, a typical dormitory building in the oil region was selected as the research object, the system equipment selection was calculated according to the relevant design specifications. On this basis, the simulation system model is established, and the evaluation index and operation control strategy suitable for the system are proposed. The energy utilization rate of the system and the economic, energy-saving, and environmental benefits of the system are simulated. The results show that, under the simulated conditions of two typical days and a heating season, the main heat load of the system is borne by the sewage source heat pump, the energy efficiency is relatively low in the cold period, and the energy-saving characteristics are not obvious. With the increase in heating temperature and anaerobic reactor volume, the energy consumption of the system also increases, and the energy efficiency ratio of each subsystem and the comprehensive energy efficiency ratio of the system gradually decrease. In addition, although the initial investment in cogeneration heating systems is high, the operating costs and environmental benefits are huge. Under the condition of maintaining 35 °C, the anaerobic reactor in the system can reduce carbon emissions by 12.15 t per year, reduce sulfur dioxide emissions by 98.4 kg, reduce dust emissions by 49.2 kg, and treat up to 2700 t of sewage per year, which has broad application prospects. Full article
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<p>Schematic diagram of multi-energy complementary combined heating system.</p>
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<p>Building floor plan.</p>
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<p>Annual heat load of the building.</p>
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<p>Simulation model of multi-energy complementary combined heating system.</p>
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<p>Logic control strategy.</p>
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<p>Sewage source heat pump unit water temperature experiments compared with the simulation data.</p>
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<p>Comparison of experimental and simulation data of return water temperature of sewage source heat pump unit.</p>
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<p>Hourly thermal loads of buildings under two typical daily conditions.</p>
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<p>Heat supply of biogas boiler subsystem of anaerobic reactor under two typical daily conditions.</p>
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<p>Energy efficiency ratio of combined heating system and heat pump energy efficiency ratio.</p>
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<p>Energy efficiency ratio of sewage source heat pump under different water supply temperatures.</p>
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<p>Energy efficiency ratio of biogas boiler subsystem of anaerobic reactor at different water supply temperatures.</p>
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<p>Comprehensive energy efficiency ratio of the system at different water supply temperatures.</p>
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<p>System heat supply at different water supply temperatures.</p>
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<p>System energy consumption at different water supply temperatures.</p>
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<p>Energy efficiency ratio of sewage source heat pump under different reactor volumes.</p>
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<p>Energy efficiency ratio of biogas boiler subsystem of anaerobic reactor under different reactor volumes.</p>
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<p>Comprehensive energy efficiency ratio of the system under different reactor volumes.</p>
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<p>Heating capacity of the system under different reactor volumes.</p>
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<p>System energy consumption under different reactor volumes.</p>
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15 pages, 4363 KiB  
Article
Comparison of Carbon-Dioxide Emissions of Diesel and LNG Heavy-Duty Trucks in Test Track Environment
by Gergő Sütheö and András Háry
Clean Technol. 2024, 6(4), 1465-1479; https://doi.org/10.3390/cleantechnol6040070 - 1 Nov 2024
Viewed by 938
Abstract
Environmental protection and greenhouse gas (GHG) emissions are getting increasingly high priority in the area of mobility. Several regulations, goals and projects have been published in recent years that clearly encourage the reduction of carbon dioxide (CO2) emission, the adoption of [...] Read more.
Environmental protection and greenhouse gas (GHG) emissions are getting increasingly high priority in the area of mobility. Several regulations, goals and projects have been published in recent years that clearly encourage the reduction of carbon dioxide (CO2) emission, the adoption of green alternatives and the use of renewable energy sources. The study compares CO2 emissions between conventional diesel and liquefied natural gas (LNG) heavy-duty vehicles (HDVs), and furthermore investigates the main influencing factors of GHG emissions. This study was carried out in a test–track environment, which supported the perfect reproducibility of the tests with minimum external influencing factors, allowing different types of measurements. At the results level, our primary objective was to collect and evaluate consumption and emission values using statistical methods, in terms of correlations, relationships and impact assessment. In this research, we recorded CO2 and pollutant emission values indirectly via the fleet management system (FMS) using controller area network (CAN) messages. Correlation, regression and statistical analyses were used to investigate the factors influencing fuel consumption and emissions. Our scientific work is a unique study in the field of HDVs, as the measurements were performed on the test track level, which provide accuracy for emission differences. The results of the project clearly show that gas technology can contribute to reducing GHG emissions of HDVs, and LNG provides a reliable alternative way forward for long-distance transportation, especially in areas of Europe where filling stations are already available. Full article
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<p>Track elements used to implement driving cycles in the ZalaZONE Proving Ground.</p>
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<p>Application of telemetry system to read CAN messages: (<b>a</b>) test process; (<b>b</b>) measurement process.</p>
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<p>Measurement results for CO<sub>2</sub> emissions (<b>a</b>) in case of diesel tractor; (<b>b</b>) in case of LNG tractor.</p>
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<p>Distribution of data—normal traffic mode. (<b>a</b>) CO<sub>2</sub> emission frequency of diesel tractor; (<b>b</b>) CO<sub>2</sub> emission and average velocity figure for diesel tractor; (<b>c</b>) CO<sub>2</sub> emission frequency of LNG tractor; (<b>d</b>) CO<sub>2</sub> emission and average velocity figure for LNG tractor.</p>
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<p>Results of the detailed statistical analysis in R Studio software (<b>a</b>) in case of diesel tractor; (<b>b</b>) in case of LNG tractor.</p>
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<p>Results of regression analysis for diesel tractor (<b>a</b>) non-linearity unequal error variances detection; (<b>b</b>) helps to find the type of distribution for random variable; (<b>c</b>) shows if residuals are spread equally along the ranges of predictions; (<b>d</b>) helps to find influential cases if there are any.</p>
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<p>Results of regression analysis for LNG tractor (<b>a</b>) non-linearity unequal error variances detection; (<b>b</b>) helps to find the type of distribution for random variable; (<b>c</b>) shows if residuals are spread equally along the ranges of predictions; (<b>d</b>) help to find influential cases if there are any.</p>
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<p>Conclusion of the regression analysis (<b>a</b>) in the case of diesel tractor; (<b>b</b>) in the case of LNG tractor.</p>
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<p>Measurements results: high load mode (<b>a</b>) in case of diesel tractor; (<b>b</b>) in case of LNG tractor.</p>
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<p>Potential future research area including relations of speed and emissions at high loads (<b>a</b>) in case of diesel tractor; (<b>b</b>) in case of LNG tractor.</p>
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20 pages, 4975 KiB  
Article
Effect of Methane on Combustion of Glycerol and Methanol Blends Using a Novel Swirl Burst Injector in a Model Dual-Fuel Gas Turbine Combustor
by S. M. Rafiul Islam, Ishaan Patel and Lulin Jiang
Clean Technol. 2024, 6(4), 1445-1464; https://doi.org/10.3390/cleantechnol6040069 - 23 Oct 2024
Viewed by 793
Abstract
Glycerol, a byproduct of biodiesel, has moderate energy but high viscosity, making clean combustion challenging. Quickly evaporating fine fuel sprays mix well with air and burn cleanly and efficiently. Unlike conventional air-blast atomizers discharging a jet core/film, a newly developed swirl burst (SB) [...] Read more.
Glycerol, a byproduct of biodiesel, has moderate energy but high viscosity, making clean combustion challenging. Quickly evaporating fine fuel sprays mix well with air and burn cleanly and efficiently. Unlike conventional air-blast atomizers discharging a jet core/film, a newly developed swirl burst (SB) injector generates fine sprays at the injector’s immediate exit, even for high-viscosity fuels, without preheating, using a unique two-phase atomization mechanism. It thus resulted in ultra-clean combustion for glycerol/methanol (G/M) blends, with complete combustion for G/M of 50/50 ratios by heat release rate (HRR). Lower combustion efficiencies were observed for G/M 60/40 and 70/30, representing crude glycerol. Hence, this study investigates the effect of premixed methane amount from 0–3 kW, and the effect of atomizing gas to liquid mass ratio (ALR) on the dual-fuel combustion efficiency of G/M 60/40-methane in a 7-kW lab-scale swirl-stabilized gas turbine combustor to facilitate crude glycerol use. Results show that more methane and increased ALR cause varying flame lift-off height, length, and gas product temperature. Regardless, mainly lean-premixed combustion, near-zero CO and NOx emissions (≤2 ppm), and ~100% combustion efficiency are enabled for all the cases by SB atomization with the assistance of a small amount of methane. Full article
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<p>(<b>a</b>) Working principle of SB injector, (<b>b</b>) SB concept [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>,<a href="#B17-cleantechnol-06-00069" class="html-bibr">17</a>,<a href="#B36-cleantechnol-06-00069" class="html-bibr">36</a>].</p>
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<p>(<b>a</b>) Schematic [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>] and (<b>b</b>) the test rig of the model dual-fuel gas turbine combustor.</p>
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<p>Flame images for (<b>a</b>) pure-liquid G/M of 60/40, and dual-fuel combustion of G/M of 60/40-methane with the methane quantity of (<b>b</b>) 0.2, (<b>c</b>) 0.4, (<b>d</b>) 0.6, (<b>e</b>) 0.8, (<b>f</b>) 1.0, (<b>g</b>) 1.5, (<b>h</b>) 2.0, (<b>i</b>) 2.5, and (<b>j</b>) 3.0 kW at a constant ER of 0.75, ALR of 3 and total HRR of 7 kW using the SB injector [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>].</p>
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<p>Axial profile of combustor outer wall surface temperature of pure-liquid G/M mix of 60/40 and G/M of 60/40-methane dual fuel combustion at a constant ER of 0.75, ALR of 3 [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>].</p>
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<p>Radial profiles of (<b>a</b>) combustion product temperature [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>] and (<b>b</b>) CO [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>], (<b>c</b>) NOx, and (<b>d</b>) CO<sub>2</sub> concentrations at the combustor exit of pure-liquid G/M mix of 60/40 and G/M of 60/40 methane dual fuel combustion at a constant total HRR of 7 kW, ER of 0.75, and ALR of 3 using the SB injector.</p>
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<p>Adiabatic flame temperature of pure-liquid G/M blend of 60/40 and G/M of 60/40 methane dual fuel combustion at a constant ER of 0.75, ALR of 3 [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>].</p>
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<p>Flame images for dual-fuel combustion of G/M (60/40)-methane (1 kW) at ALRs of (<b>a</b>) 2.0 (<b>b</b>) 2.5 and (<b>c</b>) 3.0 at a constant HRR of 7 kW and the equivalence ratio of 0.75 [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>].</p>
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<p>Axial profile of combustor outer wall surface temperature of dual-fuel combustion of G/M (60/40) methane (1 kW) for various ALRs across the SB injector at a constant ER of 0.75 [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>].</p>
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<p>Radial profiles of (<b>a</b>) combustion product temperature and concentrations of (<b>b</b>) CO and (<b>c</b>) NOx at the combustor exit of dual-fuel combustion of G/M (60/40) methane (1 kW) for various ALRs across the SB injector at a constant ER of 0.75 and a constant total air flow [<a href="#B8-cleantechnol-06-00069" class="html-bibr">8</a>].</p>
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<p>Radial profiles of (<b>a</b>) CO<sub>2</sub> and (<b>b</b>) O<sub>2</sub> emissions at the combustor exit of dual-fuel combustion of G/M (60/40)-methane (1 kW) for various ALRs across the SB injector at a constant ER of 0.75 and a constant total air flow.</p>
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14 pages, 786 KiB  
Article
An Assessment of Water Quality and Pollution Sources in a Source Region of Northwest China
by Huijuan Xin, Shuai Zhang and Weigao Zhao
Clean Technol. 2024, 6(4), 1431-1444; https://doi.org/10.3390/cleantechnol6040068 - 20 Oct 2024
Viewed by 800
Abstract
China prioritizes ensuring drinking water safety, particularly in the water-scarce northwest region. This study, utilizing water quality data from 52 village and town water sources since August 2022, assesses water quality, with a specific focus on key indicators related to organic pollution sources. [...] Read more.
China prioritizes ensuring drinking water safety, particularly in the water-scarce northwest region. This study, utilizing water quality data from 52 village and town water sources since August 2022, assesses water quality, with a specific focus on key indicators related to organic pollution sources. This study provides a scientific foundation for enhancing water quality in these sources. Employing category factor analysis for classification and grading, principal component analysis for qualitative analysis of key evaluation indicators, and the absolute principal component linear regression equation for quantitative calculation of pollution sources, this study reveals that all 52 water sources meet quality standards. Principal component analysis categorizes pollution sources as diverse types of organic compounds in surface water. Source analysis calculations highlight decay-type organic substances as major contributors to increased water color and permanganate index, with pollution contribution rates of 54.78% and 31.31%, respectively. Fecal-type organic substances dominate the increase in dissolved total solids and total coliforms, with pollution contribution rates of 56.65% and 40.16%, respectively. Additionally, high-molecular-weight organic substances exhibit lower concentrations in the water. This article presents a systematic water quality assessment methodology, which is used for the first time to qualitatively assess the types of water sources and to quantitatively trace specific sources of organic pollution in source water in northwest China. This systematic study’s results, involving initial assessment followed by traceability, recommend the adoption of a simple contact filtration and disinfection process to enhance water quality in the region. Full article
(This article belongs to the Special Issue Advanced Technologies in Drinking Water)
24 pages, 5650 KiB  
Article
Reducing Energy Consumption Using DOE and SPC on Cork Agglomeration Line
by Hugo Silva, André S. Santos and Leonilde R. Varela
Clean Technol. 2024, 6(4), 1407-1430; https://doi.org/10.3390/cleantechnol6040067 - 18 Oct 2024
Viewed by 610
Abstract
The industrial landscape has revealed two trends: increased competitiveness and a greater demand for sustainable solutions. Materials with cork in their composition are an appealing solution, since they guarantee the desired mechanical characteristics while contributing to the prevention of environmental degradation. Given the [...] Read more.
The industrial landscape has revealed two trends: increased competitiveness and a greater demand for sustainable solutions. Materials with cork in their composition are an appealing solution, since they guarantee the desired mechanical characteristics while contributing to the prevention of environmental degradation. Given the change in external factors, there has been a substantial rise in energy costs. Thus, it is essential to optimize processes, with the aim of reducing the consumption of resources, such as electricity. This project was developed at a company that manufactures cork blocks, sheets, and rolls. Regarding blocks, a critical operation of this line is the high-frequency heating, being the bottleneck of this work center. With the critical variables previously identified, planned experiments were conducted based on DOE’s full factorial methodology. Two out of four products revealed inputs with statistical significance. With these results, a reduction in parameters was implemented in the factors and interactions that showed no statistical significance. Finally, average and amplitude control charts, based on the SPC methodology, were applied to solidify and guarantee the quality of the agglomerated blocks, with the parameter changes already introduced. The company benefited from this study by having a significant reduction in its energy consumption. Full article
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<p>Cork cellular structure.</p>
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<p>Virgin cork.</p>
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<p>DMAIC phases.</p>
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<p>DOE regular application steps.</p>
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<p>X-bar chart example.</p>
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<p>Range chart example.</p>
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<p>Pareto diagram of the Compressibility of Product B.</p>
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<p>Pareto diagram of the Tensile Strength of Product B.</p>
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<p>Pareto diagram of the Compressibility of products.</p>
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<p>Pareto diagram of the Tensile Strength of Product D.</p>
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<p>X and R charts for the Compressibility of Product B.</p>
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<p>X and R charts for the Recovery of Product B.</p>
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<p>X and R charts for the Recovery of Product B with the out-of-control point removed.</p>
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<p>X and R charts for the Density of Product B.</p>
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<p>X and R charts for the Tensile Strength of Product B.</p>
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<p>X and R charts for the Compressibility of Product D.</p>
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<p>X and R charts for the Recovery of Product D.</p>
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<p>X and R charts for the Recovery of Product D with the out-of-control point removed.</p>
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<p>X and R charts for the Density of Product D.</p>
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<p>X and R charts for the Tensile Strength of Product D.</p>
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18 pages, 5073 KiB  
Article
Metal Oxalates as a CO2 Solid State Reservoir: The Carbon Capture Reaction
by Linda Pastero, Vittorio Barella, Enrico Allais, Marco Pazzi, Fabrizio Sordello, Quentin Wehrung and Alessandro Pavese
Clean Technol. 2024, 6(4), 1389-1406; https://doi.org/10.3390/cleantechnol6040066 - 14 Oct 2024
Viewed by 1010
Abstract
To maintain the carbon dioxide concentration below the no-return threshold for climate change, we must consider the reduction in anthropic emissions coupled to carbon capture methods applied in synergy. In our recent papers, we proposed a green and reliable method for carbon mineralization [...] Read more.
To maintain the carbon dioxide concentration below the no-return threshold for climate change, we must consider the reduction in anthropic emissions coupled to carbon capture methods applied in synergy. In our recent papers, we proposed a green and reliable method for carbon mineralization using ascorbic acid aqueous solution as the reducing agent for carbon (IV) to carbon (III), thus obtaining oxalic acid exploiting green reagents. Oxalic acid is made to mineralize as calcium (as the model cation) oxalate. Oxalates are solid-state reservoirs suitable for long-term carbon storage or carbon feedstock for manufacturing applications. The carbon mineralization reaction is a double-step process (carbon reduction and oxalate precipitation), and the carbon capture efficiency is invariably represented by a double-slope curve we formerly explained as a decrease in the reducing effectiveness of ascorbic acid during reaction. In the present paper, we demonstrated that the reaction proceeds via a “pure CO2-capture” stage in which ascorbic acid oxidizes into dehydroascorbic acid and carbon (IV) reduces to carbon (III) and a “mixed” stage in which the redox reaction competes with the degradation of ascorbic acid in producing oxalic acid. Despite the irreversibility of the reduction reaction, that was demonstrated in abiotic conditions, the analysis of costs according to the market price of the reagents endorses the application of the method. Full article
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<p>General trend in the carbon capture curves as determined during capture experiments (B-setup, <a href="#app1-cleantechnol-06-00066" class="html-app">Figure S1 in the Supplementary Materials</a>). The double slope was roughly associated with the kinetics of the redox reaction, i.e., fast at the initial stages when H<sub>2</sub>A-reducing power was high and then slowed down by the degradation of H<sub>2</sub>A [<a href="#B55-cleantechnol-06-00066" class="html-bibr">55</a>,<a href="#B57-cleantechnol-06-00066" class="html-bibr">57</a>].</p>
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<p>Trend of d<sup>13</sup>C measured in the mineralizing system (solid diamond-, liquid circles-, and gas squares phases) vs. time. No handling in the second run allowed a better quality of data, highlighting the first-order decay of d<sup>13</sup>C in the dissolved CO<sub>2</sub>. The points related to the d<sup>13</sup>C of the CO<sub>2</sub> from the canister and H<sub>2</sub>A (squares) are reported to be compared with the trend of the dissolved carbon. A single value for the solid fraction is reported (diamond) because of the experimental procedure intended to limit the artifacts’ appearances in the measurements as explained in the text.</p>
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<p>The general carbon capture curve via carbon mineralization into oxalates explained: in the light-grey area, the efficient pure carbon capture process during the “low-oxidation stage” of the H<sub>2</sub>A as determined by CV and LC measurements; in the dark-grey area, the mixed process of capture and H<sub>2</sub>A degradation occurring when the H<sub>2</sub>A reaches higher degree of oxidation (30–40% from CV measurements) and the H<sub>2</sub>A degradation cascade is running.</p>
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<p>Calcium oxalate is the only product of the mineralization reaction. (<b>a</b>) Calcium oxalate crystals from a B-setup carbon mineralization experiment; (<b>b</b>) XRPD pattern of the precipitate (red bars: weddellite pattern from Tazzoli and Domeneghetti, 1980 [<a href="#B105-cleantechnol-06-00066" class="html-bibr">105</a>]).</p>
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32 pages, 4014 KiB  
Article
Techno-Economic Feasibility Analysis of Post-Combustion Carbon Capture in an NGCC Power Plant in Uzbekistan
by Azizbek Kamolov, Zafar Turakulov, Patrik Furda, Miroslav Variny, Adham Norkobilov and Marcos Fallanza
Clean Technol. 2024, 6(4), 1357-1388; https://doi.org/10.3390/cleantechnol6040065 - 10 Oct 2024
Viewed by 1062
Abstract
As natural gas-fired combined cycle (NGCC) power plants continue to constitute a crucial part of the global energy landscape, their carbon dioxide (CO2) emissions pose a significant challenge to climate goals. This paper evaluates the feasibility of implementing post-combustion carbon capture, [...] Read more.
As natural gas-fired combined cycle (NGCC) power plants continue to constitute a crucial part of the global energy landscape, their carbon dioxide (CO2) emissions pose a significant challenge to climate goals. This paper evaluates the feasibility of implementing post-combustion carbon capture, storage, and utilization (CCSU) technologies in NGCC power plants for end-of-pipe decarbonization in Uzbekistan. This study simulates and models a 450 MW NGCC power plant block, a first-generation, technically proven solvent—MEA-based CO2 absorption plant—and CO2 compression and pipeline transportation to nearby oil reservoirs to evaluate the technical, economic, and environmental aspects of CCSU integration. Parametric sensitivity analysis is employed to minimize energy consumption in the regeneration process. The economic analysis evaluates the levelized cost of electricity (LCOE) on the basis of capital expenses (CAPEX) and operational expenses (OPEX). The results indicate that CCSU integration can significantly reduce CO2 emissions by more than 1.05 million tonnes annually at a 90% capture rate, although it impacts plant efficiency, which decreases from 55.8% to 46.8% because of the significant amount of low-pressure steam extraction for solvent regeneration at 3.97 GJ/tonne CO2 and multi-stage CO2 compression for pipeline transportation and subsequent storage. Moreover, the CO2 capture, compression, and transportation costs are almost 61 USD per tonne, with an equivalent LCOE increase of approximately 45% from the base case. This paper concludes that while CCSU integration offers a promising path for the decarbonization of NGCC plants in Uzbekistan in the near- and mid-term, its implementation requires massive investments due to the large scale of these plants. Full article
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<p>Current operational power plant sites in Uzbekistan (left) and the Turakurgan natural gas-fired combined cycle power plant (right).</p>
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<p>General flowsheet of the Turakurgan NGCC power plant based on [<a href="#B16-cleantechnol-06-00065" class="html-bibr">16</a>].</p>
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<p>Effects of different ratios of exhaust gas recirculation on the existing flue gas mass flow rate and the molar fractions of CO<sub>2</sub>, combustion outlet O<sub>2</sub>, and flue gas containing O<sub>2</sub>.</p>
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<p>Flue gas pre-treatment unit.</p>
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<p>The flowsheet of the capture plant model in Aspen Plus<sup>®</sup>.</p>
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<p>Relationships between the required diameter of the absorber/stripper and the number of required columns.</p>
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<p>Water-wash section flowsheet of the absorber column.</p>
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<p>Effect of water-wash section packing height on MEA and water reduction in purge gas.</p>
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<p>Sensitivity analysis workflow showing two stages. In Stage 1, the independent variables are MEA concentration (30–40 wt%), lean loading (0.15–0.30 mol/mol), and stripper pressure (1.6–2.2 bar). These variables affect the dependent variables: the diameter of both columns, required solvent flow rate, and specific reboiler duty. In Stage 2, using the results of first stage, the independent variable is the column packing height for both absorber and stripper, which affects the dependent variable, specific reboiler duty.</p>
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<p>The flowsheet of CO<sub>2</sub> dehydration, compression, and pipeline transportation to the enhanced oil recovery storage site.</p>
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<p>Relationships among lean loading (mol/mol), the required solvent flow rate, and rich loading (mol/mol) at different MEA concentrations.</p>
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<p>The relationship between lean amine loading, reboiler duty, and column diameter (both absorber and stripper) for different MEA concentrations (30%, 35%, and 40%) and at three different stripper pressures (1.6 bar, 1.8 bar, and 2 bar). Each subplot (<b>a</b>–<b>i</b>) corresponds to a specific combination of these variables.</p>
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<p>Relationships between the absorber packing height and specific booster duty and L/G ratio at 90% CO<sub>2</sub> capture efficiency.</p>
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<p>Relationship between the stripper column packing height and specific reboiler duty.</p>
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<p>Potential sites for CO<sub>2</sub> sequestration and enhanced hydrocarbon recovery [<a href="#B62-cleantechnol-06-00065" class="html-bibr">62</a>].</p>
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17 pages, 4580 KiB  
Article
Mechanisms of Water Pollutant Degradation under Electric Discharge Generated in a Cavitating Flow
by Anna Kamler, Vadim Bayazitov, Madina Sozarukova, Roman Nikonov, Igor Fedulov, Giancarlo Cravotto and Irina Abramova
Clean Technol. 2024, 6(4), 1340-1356; https://doi.org/10.3390/cleantechnol6040064 - 10 Oct 2024
Viewed by 766
Abstract
With the aim of developing an innovative water treatment approach for developing countries in the Global South, we have applied the method of treating a cavitating water stream with a plasma discharge under real conditions. To this end, we have optimised the approach [...] Read more.
With the aim of developing an innovative water treatment approach for developing countries in the Global South, we have applied the method of treating a cavitating water stream with a plasma discharge under real conditions. To this end, we have optimised the approach after investigating the effects that occur in the treated medium during such a treatment. Based on the obtained light absorption curves of treated model solutions of titanium oxysulphate and potassium bichromate, it was found that inside the reactor the main role in the destruction of chemical contaminants is played by hydroxide ions, while outside the reactor the main chemical interaction takes place with hydrogen peroxide. The plasma treatment unit was tested in the biological wastewater treatment plant of a health resort in the territory of the Russian Federation (Almetyevsk, Republic of Tatarstan). Water samples taken directly from the tertiary decantation tank were used as real wastewater samples instead of adding chemical reagents for disinfection. It was found that with different modes of operation of the plasma treatment plant, the concentration levels of coliform bacteria, coliphages and Escherichia coli decreased significantly and fell below the limit of permissible concentrations for wastewater discharge. At the same time, the possible effect of the plasma on persistent inorganic compounds was investigated. It was shown that the plasma discharge in the flow of the incoming liquid can almost completely destroy compounds that are difficult to remove, such as hydrogen sulphide and chlorides. In the course of the study, the optimum frequency of electrical pulses of 68 kHz was selected, which ensures the lowest consumption of electrical energy while maintaining the required efficiency. Full article
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<p>Experimental setup for generation of an electrical discharge in a cavitating flow: (<b>a</b>) diagram: 1—feed tank, 2—pump, 3—reactor, 4—storage tank, 5—receiving tank, 6—generator of high-frequency current pulses (power supply); (<b>b</b>) photograph of the reactor in operation.</p>
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<p>Photograph of the device during the industrial field test. On the left are the feed tank, the reactor and the waste tank. On the right is the generator of high-frequency current pulses.</p>
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<p>The second stage of aeration (<b>above</b>) and the site where water samples were taken from the tertiary decanting tank (<b>below</b>).</p>
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<p>The oscillograms of current pulses: (<b>a</b>) 40 kHz; (<b>b</b>) 55 kHz; (<b>c</b>) 68 kHz.</p>
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<p>Photo of titanium oxysulphate samples (from left to right): initial solution (1 g/L), solution after cavitation, solution after treatment with electric pulses without plasma, solution after plasma treatment and solution after dissolution in water after plasma treatment.</p>
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<p>Light absorption spectrum of titanium oxysulphate (1 g/L) after treatment (minus the initial spectrum).</p>
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<p>Photo of potassium bichromate samples (from left to right): initial solution (1 g/L), solution after cavitation, solution after treatment with electric pulses without plasma, solution after plasma treatment and solution after dissolution in water after plasma treatment.</p>
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<p>The light absorption spectrum of potassium bichromate (1 g/L) after treatment (minus the initial spectrum).</p>
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<p>Photo of titanium oxysulphate samples (from left to right): initial solution (0.01 g/L), solution after treatment with electric pulses without plasma, solution after plasma treatment and solution after dissolution in water after plasma treatment.</p>
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<p>Light absorption spectrum of titanium oxysulphate (0.01 g/L) after treatment (minus the initial spectrum).</p>
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<p>Photo of potassium bichromate samples (from left to right): initial solution (0.01 g/L), solution after treatment with electric pulses without plasma, solution after plasma treatment and solution after dissolution in water after plasma treatment.</p>
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<p>The light absorption spectrum of potassium bichromate (0.01 g/L) after treatment (minus the initial spectrum).</p>
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<p>Light absorption spectra of initial solutions of titanium oxysulphate and potassium bichromate.</p>
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<p>The spectrum of the glow of plasma burning in the flow of an incoming liquid [<a href="#B35-cleantechnol-06-00064" class="html-bibr">35</a>].</p>
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<p>An Escherichia coli cell trapped by a cavitation bubble increases in size due to an increase in internal pressure in the bubble.</p>
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14 pages, 1660 KiB  
Article
Use of Vegetable Waste for New Ecological Methods in Wool Fibre Treatments
by Simona Gavrilaș, Mihaela Dochia, Andreea-Raluca Sărsan, Bianca-Denisa Chereji and Florentina-Daniela Munteanu
Clean Technol. 2024, 6(4), 1326-1339; https://doi.org/10.3390/cleantechnol6040063 - 1 Oct 2024
Viewed by 1530
Abstract
In this current research, various amino acids (lysine, betaine, and cysteine) and peptides (oxidised or reduced glutathione) were considered as potential environmentally friendly alternatives to wool bleaching. A greener methodology was also applied to dyeing. Different agro-wastes (red cabbage, peppercorns, and red and [...] Read more.
In this current research, various amino acids (lysine, betaine, and cysteine) and peptides (oxidised or reduced glutathione) were considered as potential environmentally friendly alternatives to wool bleaching. A greener methodology was also applied to dyeing. Different agro-wastes (red cabbage, peppercorns, and red and yellow onion peels) served as raw pigment materials. The process’s efficiency was characterised by the whiteness degree, colour strength, and fastness to accelerated washing and perspiration. A higher whiteness index value was observed in the cysteine-based formulations. The onion peel exhibited significant tinctorial properties due to the presence of some natural mordants. All the proposed treatments were designed with a primary focus on environmental sustainability. These treatments offer a sustainable and environmentally friendly alternative to traditional bleaching and dyeing methods for wool. They reduce costs and energy consumption while creating added value by valorising waste. Full article
(This article belongs to the Special Issue Recovery of Bioactive Compounds from Waste and By-Products)
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<p>The natural dyeing procedure applied to wool fibres.</p>
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<p>Berger whiteness index after different bleaching treatments: w—water; cbp—cysteine and betaine + pepsin; cbHCl—cysteine and betaine + HCl; cl—cysteine and lysine; l—lysine; bp—betaine and pepsin; bHCl—betaine and HCl; c—cysteine.</p>
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<p>Berger whiteness index for different quantities of treated wool fibres under magnetic stirring: w—water; cbp—cysteine and betaine + pepsin; cbHCl—cysteine and betaine + HCl; cl—cysteine and lysine; l—lysine; bp—betaine and pepsin; bHCl—betaine and HCl; c—cysteine.</p>
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<p>Berger whiteness index of wool fibres treated with different peptidic and aminoacidic solutions: w—water; GoxbpHCl—oxidised glutathione, betaine + HCl and betaine + pepsin; GredbpHCl—reduced glutathione, betaine + HCl and betaine + pepsin; cbp—cysteine and betaine + pepsin; cbHCl—cysteine and betaine + HCl; cl—cysteine and lysine; Goxl—oxidised glutathione and lysine; Gredl—reduced glutathione and lysine; l-lysine; Goxbp—oxidised glutathione and betaine + pepsin; GoxHCl—oxidised glutathione and betaine + HCl; Gredbp-reduced glutathione and betaine + pepsin; GredHCl—reduced glutathione and betaine + HCl; bp-betaine + pepsin; bHCl-betaine + HCl; Gox—oxidised glutathione; Gred—reduced glutathione; <b>c</b>—cysteine.</p>
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<p>Perspiration colourfastness values were evaluated using the grey scale for colour differences: pm—fibres dyed with pepper and mordant; om—fibres dyed with onion and mordant; cm—fibres dyed with red cabbage and mordant; p—fibres dyed with pepper without mordant; o—fibres dyed with onion without mordant; c—fibres dyed with red cabbage without mordant.</p>
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<p>Accelerated laundering colourfastness values were evaluated using the grey scale for colour differences: pm—fibres dyed with pepper and mordant; om—fibres dyed with onion and mordant; cm—fibres dyed with red cabbage and mordant; p—fibres dyed with pepper without mordant; o—fibres dyed with onion without mordant; c—fibres dyed with red cabbage without mordant.</p>
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<p>Accelerated laundering colourfastness values were evaluated using the staining grade for colour differences evaluation: pm—fibres dyed with pepper and mordant; om—fibres dyed with onion and mordant; cm—fibres dyed with red cabbage and mordant; p—fibres dyed with pepper without mordant; o—fibres dyed with onion without mordant; c—fibres dyed with red cabbage without mordant.</p>
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<p>Colour strength was determined for all dyeing treatments used: pml—long wool fibres dyed with pepper and mordant; pl—long wool fibres dyed with pepper without mordant; pms—cut wool fibres dyed with pepper and mordant; ps—cut wool fibres dyed with pepper without mordant; oml—long wool fibres dyed with onion and mordant; ol—long wool fibres dyed with onion without mordant; oms—cut wool fibres dyed with onion and mordant; os—cut wool fibres dyed with onion without mordant; cml—long wool fibres dyed with red cabbage and mordant; cl—long wool fibres dyed with red cabbage without mordant; cms—cut wool fibres dyed with red cabbage and mordant; cs—cut wool fibres dyed with red cabbage without mordant.</p>
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