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22 pages, 3747 KiB  
Article
Macroporous Poly(hydromethylsiloxane) Networks as Precursors to Hybrid Ceramics (Ceramers) for Deposition of Palladium Catalysts
by Jan Mrówka, Robert Kosydar, Kamil Kornaus, Janusz Partyka and Magdalena Hasik
Molecules 2024, 29(16), 3808; https://doi.org/10.3390/molecules29163808 (registering DOI) - 11 Aug 2024
Abstract
Poly(hydromethylsiloxane) (PHMS) was cross-linked with 1,3,5,7-tetramethyl-1,3,5,7-tetravinylcyclotetrasiloxane (D4Vi) in water-in-oil High Internal Phase Emulsions to form macroporous materials known as polyHIPEs. It was shown that in the process of pyrolysis under Ar atmosphere at 520 °C, the obtained polyHIPEs were converted [...] Read more.
Poly(hydromethylsiloxane) (PHMS) was cross-linked with 1,3,5,7-tetramethyl-1,3,5,7-tetravinylcyclotetrasiloxane (D4Vi) in water-in-oil High Internal Phase Emulsions to form macroporous materials known as polyHIPEs. It was shown that in the process of pyrolysis under Ar atmosphere at 520 °C, the obtained polyHIPEs were converted to ceramers with high yields (82.8–88.0 wt.%). Structurally, the obtained ceramers were hybrid ceramics, i.e., they consisted of Si-O framework and preserved organic moieties. Macropores present in the polyHIPE precursors remained in ceramers. Ceramers contained also micro- and mesopores which resulted from the precursor’s mass loss during pyrolysis. Total pore volume and BET specific surface area related to the existence of micro- and mesopores in ceramers depended on the PHMS: D4Vi ratio applied in polyHIPE synthesis. The highest total pore volume (0.143 cm3/g) and specific surface area (344 m2/g) were reached after pyrolysis of the precursor prepared with the lowest amount of D4Vi as compared to PHMS. The composite materials obtained after deposition of PdO nanoparticles onto ceramers followed by reduction of PdO by H2 were active and selective catalysts for phenylacetylene hydrogenation to styrene. Full article
(This article belongs to the Special Issue Porous Materials as Catalysts and Sorbents)
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Figure 1
<p>TG and DTG curves of the studied polyHIPEs. <span class="html-italic">Note:</span> for sample symbols please refer to <a href="#sec3dot2dot1-molecules-29-03808" class="html-sec">Section 3.2.1</a>.</p>
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<p>FTIR spectra of the studied polyHIPEs (P1–P3 samples) and ceramers (C1–C3 samples). <span class="html-italic">Note:</span> for sample symbols please refer to <a href="#sec3dot2dot1-molecules-29-03808" class="html-sec">Section 3.2.1</a> and <a href="#sec3dot2dot2-molecules-29-03808" class="html-sec">Section 3.2.2</a>.</p>
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<p>DRIFT spectra recorded in situ during heating of the P3 polyHIPE under Ar atmosphere.</p>
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<p>SEM images of the materials before (P1) and after (C1) pyrolysis.</p>
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<p>Void and window size distributions in the studied polyHIPEs and ceramers determined by analysis of SEM images. <span class="html-italic">Note:</span> for sample symbols please refer to <a href="#sec3dot2dot1-molecules-29-03808" class="html-sec">Section 3.2.1</a> and <a href="#sec3dot2dot2-molecules-29-03808" class="html-sec">Section 3.2.2</a>.</p>
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<p>N<sub>2</sub> adsorption/desorption isotherms of the studied ceramers. <span class="html-italic">Note:</span> for sample symbols please refer to <a href="#sec3dot2dot2-molecules-29-03808" class="html-sec">Section 3.2.2</a>.</p>
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<p>XRD diffraction patterns of the C3 ceramer and the C3_Pd material. <span class="html-italic">Note:</span> for sample symbols please refer to <a href="#sec3dot2dot2-molecules-29-03808" class="html-sec">Section 3.2.2</a>.</p>
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<p>TPR profiles of the prepared ceramer-PdO systems. <span class="html-italic">Note:</span> for sample symbols please refer to <a href="#sec3dot2dot2-molecules-29-03808" class="html-sec">Section 3.2.2</a>.</p>
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<p>Results of phenylacetylene hydrogenation catalyzed by C1_Pd, C2_Pd and C3_Pd materials treated with H<sub>2</sub> (<b>A</b>–<b>C</b>). <span class="html-italic">Note:</span> for sample symbols please refer to <a href="#sec3dot2dot2-molecules-29-03808" class="html-sec">Section 3.2.2</a>.</p>
Full article ">
14 pages, 4295 KiB  
Article
Bio-Based Polyurethane–Urea with Self-Healing and Closed-Loop Recyclability Synthesized from Renewable Carbon Dioxide and Vanillin
by Tianyi Han, Tongshuai Tian, Shan Jiang and Bo Lu
Polymers 2024, 16(16), 2277; https://doi.org/10.3390/polym16162277 (registering DOI) - 10 Aug 2024
Viewed by 328
Abstract
Developing recyclable and self-healing non-isocyanate polyurethane (NIPU) from renewable resources to replace traditional petroleum-based polyurethane (PU) is crucial for advancing green chemistry and sustainable development. Herein, a series of innovative cross-linked Poly(hydroxyurethane-urea)s (PHUUs) were prepared using renewable carbon dioxide (CO2) and [...] Read more.
Developing recyclable and self-healing non-isocyanate polyurethane (NIPU) from renewable resources to replace traditional petroleum-based polyurethane (PU) is crucial for advancing green chemistry and sustainable development. Herein, a series of innovative cross-linked Poly(hydroxyurethane-urea)s (PHUUs) were prepared using renewable carbon dioxide (CO2) and vanillin, which displayed excellent thermal stability properties and solvent resistance. These PHUUs were constructed through the introduction of reversible hydrogen and imine bonds into cross-linked polymer networks, resulting in the cross-linked PHUUs exhibiting thermoplastic-like reprocessability, self healing, and closed-loop recyclability. Notably, the results indicated that the VL-TTD*-50 with remarkable hot-pressed remolding efficiency (nearly 98.0%) and self-healing efficiency (exceeding 95.0%) of tensile strength at 60 °C. Furthermore, they can be degraded in the 1M HCl and THF (v:v = 2:8) solution at room temperature, followed by regeneration without altering their original chemical structure and mechanical properties. This study presents a novel strategy for preparing cross-linked PHUUs with self-healing and closed-loop recyclability from renewable resources as sustainable alternatives for traditional petroleum-based PUs. Full article
(This article belongs to the Special Issue Preparation and Application of Biodegradable Polymeric Materials)
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Figure 1
<p>Schematic structure of VL-TTD* elastomers.</p>
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<p>(<b>a</b>) FTIR spectra of VL−C and VL−TTD*s; (<b>b</b>) FTIR spectra of VL−TTD*s; (<b>c</b>) swelling rates of the VL−TTD*s; (<b>d</b>) gel contents of the VL−TTD*s.</p>
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<p>Temperature-dependent <sup>1</sup>H NMR spectra of VL-TTD*-50 upon heating from 30 to 100 °C (<b>a</b>) and upon cooling from 100 to 30 °C (<b>b</b>).</p>
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<p>The rheology of VL-TTD*s: (<b>a</b>) Variation in the storage modulus as a function of the frequency and (<b>b</b>) variation in the loss modulus as a function of the frequency.</p>
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<p>(<b>a</b>) TGA and DTG curves of VL-TTD*s in N<sub>2</sub>; (<b>b</b>) DSC curves of VL-TTD*s; (<b>c</b>) stress–strain curves of VL-TTD*s; (<b>d</b>) mechanical properties of VL-TTD*s.</p>
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<p>(<b>a</b>) Photographs of the hot-pressing process. (<b>b</b>) FT-IR spectra of VL-TTD*-50 after two recycling processes; (<b>c</b>) stress–strain curves of VL-TTD*-50 after two recycling processes.</p>
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<p>(<b>a</b>) Polarizing optical microscopy images of the self-healing process of a crack on the VL-TTD*-50; (<b>b</b>) images of the self-healing of VL-TTD*-50: (i) original sample; (ii) cut segments; (iii) healed sample; (iv) the healed sample with the hanging weight of a 500 g bottle; (<b>c</b>) stress–strain curves of the VL-TTD*-50 after healing at different times.</p>
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<p>The self-healing mechanism of the VL-TTD*s.</p>
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<p>Closed-loop recycling of VL-TTD*s.</p>
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<p>(<b>a</b>) Degradation rate curves of VL-TTD*-50 in 1M HCl and THF (<span class="html-italic">v</span>:<span class="html-italic">v</span> = 2:8) and H<sub>2</sub>O/THF (<span class="html-italic">v</span>:<span class="html-italic">v</span> = 2:8); (<b>b</b>) FT-IR spectra of VL-TTD*-50, degraded products, and regenerated VL-TTD*-50; (<b>c</b>) stress–strain curves of original and regenerated VL-TTD*-50; (<b>d</b>) DSC curves of original and regenerated VL-TTD*-50.</p>
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<p>Synthetic routes of the VL-TTD*s.</p>
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11 pages, 2207 KiB  
Article
The Effect of α-Fe2O3(0001) Surface Containing Hydroxyl Radicals and Ozone on the Formation Mechanism of Environmentally Persistent Free Radicals
by Danli Liang, Jiarong Liu, Chunlin Wang, Kaipeng Tu, Li Wang, Lili Qiu, Xiuhui Zhang and Ling Liu
Toxics 2024, 12(8), 582; https://doi.org/10.3390/toxics12080582 (registering DOI) - 10 Aug 2024
Viewed by 278
Abstract
The formation of environmentally persistent free radicals (EPFRs) is mediated by the particulate matter's surface, especially transition metal oxide surfaces. In the context of current atmospheric complex pollution, various atmospheric components, such as key atmospheric oxidants ·OH and O3, are often [...] Read more.
The formation of environmentally persistent free radicals (EPFRs) is mediated by the particulate matter's surface, especially transition metal oxide surfaces. In the context of current atmospheric complex pollution, various atmospheric components, such as key atmospheric oxidants ·OH and O3, are often absorbed on particulate matter surfaces, forming particulate matter surfaces containing ·OH and O3. This, in turn, influences EPFRs formation. Here, density functional theory (DFT) calculations were used to explore the formation mechanism of EPFRs by C6H5OH on α-Fe2O3(0001) surface containing the ·OH and O3, and compare it with that on clean surface. The results show that, compared to EPFRs formation with an energy barrier on a clean surface, EPFRs can be rapidly formed through a barrierless process on these surfaces. Moreover, during the hydrogen abstraction mechanism leading to EPFRs formation, the hydrogen acceptor shifts from a surface O atom on a clean surface to an O atom of ·OH or O₃ on these surfaces. However, the detailed hydrogen abstraction process differs on surfaces containing oxidants: on surfaces containing ·OH, it occurs directly through a one-step mechanism, while, on surfaces containing O3, it occurs through a two-step mechanism. But, in both types of surfaces, the essence of this promotional effect mainly lies in increasing the electron transfer amounts during the reaction process. This research provides new insights into EPFRs formation on particle surfaces within the context of atmospheric composite pollution. Full article
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<p>The energy profile for the reaction of C<sub>6</sub>H<sub>5</sub>OH on the α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing ·OH together with the corresponding structures. Energy is in kJ/mol, and bond length is in Å. Color code: Fe (blue), C (gray), O (red), and H (white). Line: O1-H1 (red line), O2-H1 (black line).</p>
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<p>The energy profile for the reaction of C<sub>6</sub>H<sub>5</sub>OH on the α-Fe<sub>2</sub>O<sub>3</sub>(0001)) surface containing O<sub>3</sub> together with the corresponding structures. Energy is in kJ/mol, and bond length is in Å. Color code: Fe (blue), C (gray), O (red), and H (white). Line: O1-H1 (red line), O2-H1 (black line).</p>
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<p>The adsorption energy of C<sub>6</sub>H<sub>5</sub>OH on the different surfaces: (<b>a</b>) clean α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface, (<b>b</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing ·OH and (<b>c</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing O<sub>3</sub>. Energy is in kJ/mol.</p>
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<p>The amount of electron transfer during EPFRs formation: (<b>a</b>) clean α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface, (<b>b</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing ·OH, and (<b>c</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing O<sub>3</sub>.</p>
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<p>The amount of electron transfer of surface on the different surfaces: (<b>a</b>) clean α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface, (<b>b</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing ·OH, and (<b>c</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing O<sub>3</sub>.</p>
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<p>The amount of electron transfer of Fe site on the different surfaces: (<b>a</b>) clean α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface, (<b>b</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing ·OH, and (<b>c</b>) α-Fe<sub>2</sub>O<sub>3</sub>(0001) surface containing O<sub>3</sub>.</p>
Full article ">
43 pages, 3341 KiB  
Review
New Insights Regarding the Use of Relevant Synthetic Compounds in Dentistry
by Stefania-Irina Dumitrel, Anamaria Matichescu, Stefania Dinu, Roxana Buzatu, Ramona Popovici, Dorin Cristian Dinu and Dana Cristina Bratu
Molecules 2024, 29(16), 3802; https://doi.org/10.3390/molecules29163802 (registering DOI) - 10 Aug 2024
Viewed by 243
Abstract
Worldwide, synthetic compounds are used for both in-office and at-home dental care. They are a valuable resource for both prophylactic and curative treatments for various dental problems, such as tooth decay, periodontal diseases, and many more. They are typically preferred due to their [...] Read more.
Worldwide, synthetic compounds are used for both in-office and at-home dental care. They are a valuable resource for both prophylactic and curative treatments for various dental problems, such as tooth decay, periodontal diseases, and many more. They are typically preferred due to their broad range of actions and ability to produce targeted, rapid, and long-lasting effects. Using a 0.12% chlorhexidine mouthwash is capable of reducing the plaque index from 47.69% to 2.37% and the bleeding index from 32.93% to 6.28% after just 2 weeks. Mouthwash with 0.1% OCT is also highly effective, as it significantly lowered the median plaque index and salivary bacterial counts in 152 patients in 5 days compared to a control group (p < 0.0001), while also reducing the gingival index (p < 0.001). When povidone-iodine was used as an irrigant during the surgical removal of mandibular third molars in 105 patients, it resulted in notably lower pain scores after 2 days compared to a control group (4.57 ± 0.60 vs. 5.71 ± 0.45). Sodium hypochlorite is excellent for root canal disinfection, as irrigating with 1% NaOCl completely eliminated the bacteria from canals in 65% patients. A 0.05% CPC mouthwash proved effective for perioperative patient care, significantly decreasing gingival bleeding (p < 0.001) and suppressing Streptococcus levels even one week post-surgery. Lastly, a 6% H2O2 paint-on varnish and 6% H2O2 tray formulations successfully bleached the teeth of 40 patients, maintaining a noticeably whiter appearance up to the 6-month follow-up, with significant color differences from the baseline (p < 0.005). Synthetic compounds have a large research base, which also provides a greater awareness of their mechanism of action and potential adverse effects. For a better understanding of how they work, several methods and assays are performed. These are protocolary techniques through which a compound’s efficacy and toxicity are established. Full article
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<p>The molecular structure of chlorhexidine.</p>
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<p>The mechanism of action of chlorhexidine.</p>
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<p>The molecular structure of octenidine.</p>
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<p>The mechanism of action of octenidine.</p>
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<p>The molecular structure of povidone-iodine.</p>
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<p>The mechanism of action of povidone-iodine.</p>
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<p>The molecular structure of sodium hypochlorite.</p>
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<p>The mechanism of action of sodium hypochlorite.</p>
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<p>Molecular structure of cetylpyridinium chloride.</p>
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<p>The mechanism of action of cetylpiridinium chloride.</p>
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<p>Molecular structure of hydrogen peroxide.</p>
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<p>The mechanism of action of hydrogen peroxide.</p>
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28 pages, 3497 KiB  
Review
Polymer-Assisted Graphite Exfoliation: Advancing Nanostructure Preparation and Multifunctional Composites
by Jaime Orellana, Esteban Araya-Hermosilla, Andrea Pucci and Rodrigo Araya-Hermosilla
Polymers 2024, 16(16), 2273; https://doi.org/10.3390/polym16162273 (registering DOI) - 10 Aug 2024
Viewed by 374
Abstract
Exfoliated graphite (ExG) embedded in a polymeric matrix represents an accessible, cost-effective, and sustainable method for generating nanosized graphite-based polymer composites with multifunctional properties. This review article analyzes diverse methods currently used to exfoliate graphite into graphite nanoplatelets, few-layer graphene, and polymer-assisted graphene. [...] Read more.
Exfoliated graphite (ExG) embedded in a polymeric matrix represents an accessible, cost-effective, and sustainable method for generating nanosized graphite-based polymer composites with multifunctional properties. This review article analyzes diverse methods currently used to exfoliate graphite into graphite nanoplatelets, few-layer graphene, and polymer-assisted graphene. It also explores engineered methods for small-scale pilot production of polymer nanocomposites. It highlights the chemistry involved during the graphite intercalation and exfoliation process, particularly emphasizing the interfacial interactions related to steric repulsion forces, van der Waals forces, hydrogen bonds, π-π stacking, and covalent bonds. These interactions promote the dispersion and stabilization of the graphite derivative structures in polymeric matrices. Finally, it compares the enhanced properties of nanocomposites, such as increased thermal and electrical conductivity and electromagnetic interference (EMI) shielding applications, with those of neat polymer materials. Full article
(This article belongs to the Special Issue Functional Graphene-Polymer Composites)
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<p>Graphite structures and sources.</p>
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<p>SEM micrographs of rolling intercalation PS with 5% of colloidal graphite [<a href="#B27-polymers-16-02273" class="html-bibr">27</a>]. Reproduced with permission from Tu, H.; Polymers for advanced technologies; Published by John/Wiley &amp; Sons Ltd.; 2008.</p>
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<p>Orientation of the graphite platelet structures in extruded strands: (left) schematic figure of platelet orientation along strand flow direction by extrusion out of the die; and (right) transmission light microscopy pictures of samples cut perpendicular to the strand direction (shows mainly the layer thickness) and cut parallel to the long-axis of the strand (shows the lateral dimension of visible GNP structures), here shown for 1 wt% Graphene nanopowder AO-3 in PC [<a href="#B124-polymers-16-02273" class="html-bibr">124</a>]. Reproduced with permission from Pötschke, P.; Materials; Published by MDPI; 2017.</p>
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<p>SEM images of (<b>a</b>) PVDF/expanded graphite composite fabricated without water (P-EG) and (<b>b</b>) PVDF/expanded graphite composite fabricated with water (P-EG-W) samples [<a href="#B91-polymers-16-02273" class="html-bibr">91</a>]. Reproduced with permission from Tong, J.; Macromolecular materials and engineering; Published by Wiley-VCH Verlag GMBH &amp; Co.; 2020.</p>
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<p>FESEM images of (<b>A</b>) PCGF-30 [<a href="#B87-polymers-16-02273" class="html-bibr">87</a>]. Reproduced with permission from Pradhan, S.S.; Polymer composites; Published by John/Wiley &amp; Sons Ltd.; 2021.</p>
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<p>SEM images of graphite at magnifications of 15 and 150 Kx at different ball milling times: (<b>a</b>,<b>b</b>) 0 h; (<b>c</b>,<b>d</b>) 1 h; (<b>e</b>,<b>f</b>) 4 h; (<b>g</b>,<b>h</b>) 8 h; (<b>i</b>,<b>j</b>) 16 h [<a href="#B130-polymers-16-02273" class="html-bibr">130</a>]. Reproduced with permission from Visco, A.; Polymers; Published by MDPI; 2021.</p>
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<p>EMI-S effectiveness (dB) and wt% filler in different matrix.</p>
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<p>Thermal conductivity and wt% filler in different matrix, conductive nanocomposite.</p>
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<p>Thermal conductivity and wt% filler in different matrices, conductive nanocomposite.</p>
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<p>Engineering state-of-the-art techniques to generate exfoliated graphite/polymers composites.</p>
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21 pages, 2184 KiB  
Review
A Review of Life Cycle Assessment (LCA) Studies for Hydrogen Production Technologies through Water Electrolysis: Recent Advances
by Negar Shaya and Simon Glöser-Chahoud
Energies 2024, 17(16), 3968; https://doi.org/10.3390/en17163968 (registering DOI) - 10 Aug 2024
Viewed by 247
Abstract
Climate change is a major concern for the sustainable development of global energy systems. Hydrogen produced through water electrolysis offers a crucial solution by storing and generating renewable energy with minimal environmental impact, thereby reducing carbon emissions in the energy sector. Our research [...] Read more.
Climate change is a major concern for the sustainable development of global energy systems. Hydrogen produced through water electrolysis offers a crucial solution by storing and generating renewable energy with minimal environmental impact, thereby reducing carbon emissions in the energy sector. Our research evaluates current hydrogen production technologies, such as alkaline water electrolysis (AWE), proton exchange membrane water electrolysis (PEMWE), solid oxide electrolysis (SOEC), and anion exchange membrane water electrolysis (AEMWE). We systematically review life cycle assessments (LCA) for these technologies, analyzing their environmental impacts and recent technological advancements. This study fills essential gaps by providing detailed LCAs for emerging technologies and evaluating their scalability and environmental footprints. Our analysis outlines the strengths and weaknesses of each technology, guiding future research and assisting stakeholders in making informed decisions about integrating hydrogen production into the global energy mix. Our approach highlights operational efficiencies and potential sustainability enhancements by employing comparative analyses and reviewing advancements in membrane technology and electrocatalysts. A significant finding is that PEMWE when integrated with renewable energy sources, offers rapid response capabilities that are vital for adaptive energy systems and reducing carbon footprints. Full article
(This article belongs to the Section A5: Hydrogen Energy)
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<p>The different technologies for hydrogen production are based on the energy source employed and inspired by [<a href="#B15-energies-17-03968" class="html-bibr">15</a>,<a href="#B16-energies-17-03968" class="html-bibr">16</a>].</p>
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<p>Schematic figure of the AWE cell according to [<a href="#B15-energies-17-03968" class="html-bibr">15</a>].</p>
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<p>Schematic figure of the AEMWE cell according to [<a href="#B15-energies-17-03968" class="html-bibr">15</a>,<a href="#B33-energies-17-03968" class="html-bibr">33</a>].</p>
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<p>Schematic figure of the SOEC according to [<a href="#B15-energies-17-03968" class="html-bibr">15</a>].</p>
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<p>Schematic figure of the PEMWE cell according to [<a href="#B15-energies-17-03968" class="html-bibr">15</a>,<a href="#B33-energies-17-03968" class="html-bibr">33</a>].</p>
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<p>GWP comparison across different electrolysis systems.</p>
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<p>Eutrophication potential comparison across different electrolyzer technologies.</p>
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<p>Acidification potential comparison across different electrolyzer technologies.</p>
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20 pages, 5453 KiB  
Article
Influence of Synthesis Conditions on Catalytic Performance of Ni/CeO2 in Aqueous-Phase Hydrogenolysis of Glycerol without External Hydrogen Input
by Clara Jarauta-Córdoba, Lucía García, Joaquín Ruiz, Miriam Oliva and Jesús Arauzo
Molecules 2024, 29(16), 3797; https://doi.org/10.3390/molecules29163797 (registering DOI) - 10 Aug 2024
Viewed by 197
Abstract
The aqueous-phase hydrogenolysis of glycerol was studied in Ni/CeO2 catalytic systems prepared by incipient wetness impregnation. The operating conditions were 34 bar, 227 ºC, 5 wt.% of glycerol, and a W/mglycerol = 20 g catalyst min/g glycerol without a hydrogen supply. [...] Read more.
The aqueous-phase hydrogenolysis of glycerol was studied in Ni/CeO2 catalytic systems prepared by incipient wetness impregnation. The operating conditions were 34 bar, 227 ºC, 5 wt.% of glycerol, and a W/mglycerol = 20 g catalyst min/g glycerol without a hydrogen supply. The effect of the catalyst preparation conditions on the catalytic activity and physicochemical properties of the catalysts was assessed, particularly the calcination temperature of the support, the calcination temperature of the catalyst, and the Ni content. The physicochemical properties of the catalysts were determined by N2 adsorption, H2-TPR, NH3-TPD, and XRD, among other techniques. A relevant increase in acidity was observed when increasing the nickel content up to 20 wt.%. The increase in the calcination temperatures of the supports and catalysts showed a detrimental effect on the specific surface area and acid properties of the catalysts, which were crucial to the selectivity of the reaction. These catalysts notably enhanced the yield of liquid products, achieving global glycerol conversion values ranging from 17.1 to 29.0% and carbon yield to liquids ranging from 12.6 to 24.0%. Acetol and 1,2-propanediol were the most abundant products obtained in the liquid stream. Full article
(This article belongs to the Topic Biomass for Energy, Chemicals and Materials)
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<p>Effect of (<b>a</b>) calcination temperature and (<b>b</b>) Ni content on pore volume distribution.</p>
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<p>XRD patterns of CeO<sub>2</sub> supports: (<b>a</b>) CeO<sub>2</sub>(500) and (<b>b</b>) CeO<sub>2</sub>(700).</p>
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<p>XRD diffractograms of calcined (<b>left</b>) and reduced (<b>right</b>) catalysts: (<b>a</b>) Ni10/CeO<sub>2</sub>(500)600, (<b>b</b>) Ni10/CeO<sub>2</sub>(500)700, (<b>c</b>) Ni10/CeO<sub>2</sub>(500)800, (<b>d</b>) Ni10/CeO<sub>2</sub>(700)700, and (<b>e</b>) Ni20/CeO<sub>2</sub>(500)700.</p>
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<p>H<sub>2</sub>-TPR profiles of CeO<sub>2</sub> supports (<b>left</b>): (<b>a</b>) CeO<sub>2</sub>(500) and (<b>b</b>) CeO<sub>2</sub>(700); H<sub>2</sub>-TPR profiles of Ni/CeO<sub>2</sub> catalysts (<b>right</b>): (<b>a</b>) Ni10/CeO<sub>2</sub>(500)600, (<b>b</b>) Ni10/CeO<sub>2</sub>(500)700, (<b>c</b>) Ni10/CeO<sub>2</sub>(500)800, (<b>d</b>) Ni10/CeO<sub>2</sub>(700)700, and (<b>e</b>) Ni20/CeO<sub>2</sub>(500)700.</p>
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<p>NH<sub>3</sub>-TPD profiles of CeO<sub>2</sub> supports (<b>left</b>): (<b>a</b>) CeO<sub>2</sub>(500) and (<b>b</b>) CeO<sub>2</sub>(700); NH<sub>3</sub>-TPD profiles of Ni/CeO<sub>2</sub> catalysts (<b>right</b>): (<b>a</b>) Ni10/CeO<sub>2</sub>(500)600, (<b>b</b>) Ni10/CeO<sub>2</sub>(500)700, (<b>c</b>) Ni10/CeO<sub>2</sub>(500)800, (<b>d</b>) Ni10/CeO<sub>2</sub>(700)700, and (<b>e</b>) Ni20/CeO<sub>2</sub>(500)700.</p>
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<p>Effect of specific surface on the catalytic acidity (expressed on a mass basis).</p>
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<p>Catalytic activity results.</p>
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<p>Variation of CCliq (%) from the third to the first hour of reaction.</p>
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<p>Reaction pathway: glycerol conversion to 1,2-PDO and EG.</p>
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<p>Acidity effects on the selectivity towards main products.</p>
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<p>XRD diffractograms of spent Ni/CeO<sub>2</sub> catalysts: (<b>a</b>) Ni10/CeO<sub>2</sub>(500)600, (<b>b</b>) Ni10/CeO<sub>2</sub>(500)700, (<b>c</b>) Ni10/CeO<sub>2</sub>(500)800, (<b>d</b>) Ni10/CeO<sub>2</sub>(700)700, and (<b>e</b>) Ni20/CeO<sub>2</sub>(500)700.</p>
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<p>SEM images: (<b>a</b>) calcined Ni10/CeO<sub>2</sub>(500)700, (<b>b</b>) used after reaction Ni10/CeO<sub>2</sub>(500)700, (<b>c</b>) calcined Ni10/CeO<sub>2</sub>(500)800, and (<b>d</b>) used after reaction Ni10/CeO<sub>2</sub>(500)800.</p>
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19 pages, 1461 KiB  
Article
Effect of Polyethylene Glycol with Different Molecular Weights on the Properties of Mytilaria laosensis Timber
by Linhan He, Xiaoling Liu, Yin Kuang, Liuliu Wang, Songwu Chen, Yufen Luo and Yao Chen
Forests 2024, 15(8), 1401; https://doi.org/10.3390/f15081401 (registering DOI) - 10 Aug 2024
Viewed by 151
Abstract
Mytilaria laosensis, a common fast-growing tree species in southern China, boasts excellent growth speed and attractive color and texture. However, due to its short growth cycle and high proportion of juvenile wood, it typically exhibits poor dimensional stability and low strength, which [...] Read more.
Mytilaria laosensis, a common fast-growing tree species in southern China, boasts excellent growth speed and attractive color and texture. However, due to its short growth cycle and high proportion of juvenile wood, it typically exhibits poor dimensional stability and low strength, which significantly limits its practical applications. This study uses vacuum impregnation to modify M. laosensis wood with polyethylene glycol (PEG), focusing on the effects and mechanisms of PEG with different molecular weights on wood properties. The results indicate that PEG enters the wood cell walls through capillary action and diffusion, forming hydrogen bonds with the free hydroxyl groups on cellulose and hemicellulose, which keeps the cell walls swollen and enhances dimensional stability. Post modification, the dimensional stability of M. laosensis wood improved, with an anti-swelling efficiency ranging from 61.43% to 71.22%, showing an initial increase followed by a decrease with increasing PEG molecular weight. The optimal PEG molecular weight for anti-swelling efficiency was 1500 Da, achieving 71.22%. The flexural modulus of elasticity and flexural strength of the treated wood also first decreased and then increased with increasing PEG molecular weight. Among them, the PEG1000-treated material showed the best performance, with the flexural modulus of elasticity increased by about 29% and the flexural strength increased by about 5% compared to untreated wood. Additionally, PEG, having a higher pyrolysis temperature than wood, raised the initial pyrolysis temperature and maximum pyrolysis rate temperature of M. laosensis wood, thus improving its thermal stability. These findings provide scientific evidence and technical support for the efficient utilization and industrialization of M. laosensis wood, promoting its widespread application and industrial development. Full article
(This article belongs to the Section Wood Science and Forest Products)
17 pages, 1811 KiB  
Article
Thermodynamic Exercises for the Kinetically Controlled Hydrogenation of Carvone
by Artemiy A. Samarov, Sergey V. Vostrikov, Aleksandr P. Glotov and Sergey P. Verevkin
Chemistry 2024, 6(4), 706-722; https://doi.org/10.3390/chemistry6040042 (registering DOI) - 10 Aug 2024
Viewed by 107
Abstract
Carvone belongs to the chemical family of terpenoids and is the main component of various plant oils. Carvone and its hydrogenated products are used in the flavouring and food industries. A quantitative thermodynamic analysis of the general network of carvone hydrogenation reactions was [...] Read more.
Carvone belongs to the chemical family of terpenoids and is the main component of various plant oils. Carvone and its hydrogenated products are used in the flavouring and food industries. A quantitative thermodynamic analysis of the general network of carvone hydrogenation reactions was performed based on the thermochemical properties of the starting carvone and all possible intermediates and end products. The enthalpies of vaporisation, enthalpies of formation, entropies and heat capacities of the reactants were determined by complementary measurements and a combination of empirical, theoretical and quantum chemical methods. The energetics and entropy change in the hydrogenation and isomerisation reactions that take place during the conversion of carvone were derived, and the Gibbs energies of the reactions were estimated. It was shown that negative Gibbs energies are recorded for all reactions that may occur during the hydrogenation of carvone, although these differ significantly in magnitude. This means that all these reactions are thermodynamically feasible in a wide range from ambient temperature to elevated temperatures. Therefore, all these reactions definitely take place under kinetic and not thermodynamic control. Nevertheless, the numerical Gibbs energy values can help to establish the chemoselectivity of catalysts used to convert carvone to either carvacarol or to dihydro- and terahydrocarvone, either in carvotanacetone or carveol. Full article
(This article belongs to the Section Theoretical and Computational Chemistry)
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<p>General network of carvone hydrogenation reactions.</p>
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<p>Cis-trans isomerisation of the carvone derivatives as a concomitant of carvone hydrogenation reactions.</p>
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<p>Structures of the most stable conformers of carvone (CAS 99-49-0) as calculated using the G4 method.</p>
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<p>Calculating of <math display="inline"><semantics> <mrow> <msubsup> <mrow> <mo>∆</mo> </mrow> <mrow> <mi mathvariant="normal">l</mi> </mrow> <mrow> <mi mathvariant="normal">g</mi> </mrow> </msubsup> <msubsup> <mrow> <mi>H</mi> </mrow> <mrow> <mi mathvariant="normal">m</mi> </mrow> <mrow> <mi mathvariant="normal">o</mi> </mrow> </msubsup> </mrow> </semantics></math>(298 K). Development of the contribution H→iPr(en) for the exchange of the H-atom in the cyclohexane ring for the iso-propenyl substituent (<b>left</b>). Development of the contribution H→iPr for the exchange of the H-atom in the cyclohexane ring for the iso-propyl substituent (<b>right</b>). All values in kJ·mol<sup>−1</sup>.</p>
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<p>Calculation of the enthalpy of vaporisation, <math display="inline"><semantics> <mrow> <msubsup> <mrow> <mo>∆</mo> </mrow> <mrow> <mi mathvariant="normal">l</mi> </mrow> <mrow> <mi mathvariant="normal">g</mi> </mrow> </msubsup> <msubsup> <mrow> <mi>H</mi> </mrow> <mrow> <mi mathvariant="normal">m</mi> </mrow> <mrow> <mi mathvariant="normal">o</mi> </mrow> </msubsup> </mrow> </semantics></math>(298 K), of carvone using the 2-methyl-2-cyclohexen-1-one as the “centrepiece” (<b>left</b>). Calculation the enthalpy of vaporisation, <math display="inline"><semantics> <mrow> <msubsup> <mrow> <mo>∆</mo> </mrow> <mrow> <mi mathvariant="normal">l</mi> </mrow> <mrow> <mi mathvariant="normal">g</mi> </mrow> </msubsup> <msubsup> <mrow> <mi>H</mi> </mrow> <mrow> <mi mathvariant="normal">m</mi> </mrow> <mrow> <mi mathvariant="normal">o</mi> </mrow> </msubsup> </mrow> </semantics></math>(298 K), of tetrahydrocarvone using the 2-methyl-cyclohexanone as the “centrepiece” (<b>right</b>). All values in kJ·mol<sup>−1</sup>. The experimental values of vaporisation enthalpies of the “centrepieces” are given in <a href="#app1-chemistry-06-00042" class="html-app">Tables S2 and S5</a>.</p>
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<p>Reactions of the partial and complete hydrogenation of double bonds in carvone and carvacrol (reactions 16–18 in <a href="#chemistry-06-00042-t005" class="html-table">Table 5</a>).</p>
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23 pages, 5105 KiB  
Article
The Influence of Hydrogen Addition on a SI Engine—Theoretical and Experimental Investigations
by Rareș Georgescu, Constantin Pană, Niculae Negurescu, Alexandru Cernat, Cristian Nuțu and Cristian Sandu
Sustainability 2024, 16(16), 6873; https://doi.org/10.3390/su16166873 (registering DOI) - 10 Aug 2024
Viewed by 225
Abstract
In a world with severe pollution regulations and restrictions imposed to internal combustion engines, improving efficiency and reducing pollutant emissions and greenhouse gases are important goals for researchers. A highly effective method to achieve the premises written above is to use alternative fuels, [...] Read more.
In a world with severe pollution regulations and restrictions imposed to internal combustion engines, improving efficiency and reducing pollutant emissions and greenhouse gases are important goals for researchers. A highly effective method to achieve the premises written above is to use alternative fuels, which may have a strong influence on combustion processes in spark ignition engines. In order to increase the heat release rate during combustion, the brake thermal efficiency, and to decrease the levels of pollutant emissions and greenhouse gases, the use of sustainable alternative fuels, in parallel with conventional fuels is a great choice. Among alternative fuels, hydrogen is an excellent fuel in terms of its physical-chemical properties, making it an attractive replacement for classic fuels in the combustion process. This article demonstrates AMESim 13.0.0/Rev13 theoretical and experimental investigations conducted on a supercharged spark ignition engine at 55% engine load and 2500 rpm speed, analyzes the effect of 2.15% hydrogen that substitutes gasoline on combustion, implicitly investigates energy and fuel efficiency of the engine and investigates pollutant and greenhouse gas emission levels. These experimental investigations confirm the theoretical study of thermo-gas-dynamic processes of a SI engine fueled with gasoline and hydrogen, and it shows the importance of engine tunings and hydrogen quantity on engine operation. The obtained results indicate the advantages of fueling the engine with both gasoline and hydrogen: the increase of the heat release rate which leads to the increase of maximum pressure and maximum pressure rise rate during combustion, the increase of the brake thermal efficiency, the decrease of the combustion duration, the decrease of the brake specific energetic consumption by 4.8%, the decrease of the levels of pollutant emissions by 11.11% for unburned hydrocarbons HC, by 12.5% for monoxide carbon CO, by 63.23% for nitrogen oxides NOx, and by 33.7% for carbon dioxide CO2 as a greenhouse gas. Further research directions can be developed from this research for other operating regimes and other hydrogen quantities. Full article
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<p>The experimental test bench of the A15MF engine. 1—gas analyzer, 2—intake turbocharger pressure sensor, 3—control cabinet for dynamometer, 4—AVL Dynoperform 160 eddy current dynamometer, 5—gasoline injectors, 6—Krohne Optimass flowmeter for gasoline, 7—fuel tank for gasoline, 8—hydrogen tank, 9—hydrogen pressure regulator, 10—Alicat Scientific MC50 flowmeter for hydrogen, 11—flame trap, 12—hydrogen injectors, 13—AVL piezoelectric charge amplifier, 14—AVL Indimodul 621 data acquisition system, 15—data acquisition system computer, 16—cabinet for fine tune of injection system, 17—computer equipped with Dastek Unichip software 1.0 for fueling systems tune, 18—engine ECU, 19—A15MF spark ignition engine, 20—inlet air flowmeter, 21—intake air tank.</p>
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<p>The numeric engine schema designed in AMESim: 1—throttle body, 2—fuel injector, 3—cylinder, 4—crank shaft.</p>
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<p>In-cylinder pressure diagrams from the experimental study.</p>
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<p>Maximum pressure from the experimental study.</p>
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<p>Maximum pressure rise rate from the experimental study.</p>
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<p>Heat release rate diagrams from the experimental study.</p>
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<p>Heat release laws from the experimental study.</p>
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<p>Total combustion duration as determined from the experimental study.</p>
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<p>The brake specific energy consumption from the experimental study.</p>
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<p>The HC emission level from the experimental study.</p>
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<p>The CO emission levels from the experimental study.</p>
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<p>The CO<sub>2</sub> emission levels from the experimental study.</p>
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<p>The NO<sub>x</sub> emission level from the experimental study.</p>
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<p>Pressure diagrams of the theoretical and experimental studies of gasoline fueling and gasoline-hydrogen (2.15%) fueling, at stoichiometric dosage.</p>
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<p>Theoretical and experimental diagrams of the heat release rate of gasoline fueling and gasoline-hydrogen (2.15%) fueling, at stoichiometric dosage.</p>
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<p>Theoretical and experimental diagrams of the combustion laws for gasoline fueling and gasoline-hydrogen (2.15%), at stoichiometric dosage.</p>
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15 pages, 1277 KiB  
Article
Fast-Neutron Radiolysis of Sub- and Supercritical Water at 300–600 °C and 25 MPa: A Monte Carlo Track Chemistry Simulation Study
by Md Shakhawat Hossen Bhuiyan, Jintana Meesungnoen, Abida Sultana and Jean-Paul Jay-Gerin
Appl. Sci. 2024, 14(16), 7024; https://doi.org/10.3390/app14167024 (registering DOI) - 10 Aug 2024
Viewed by 204
Abstract
(1) Background: Supercritical water-cooled reactors (SCWRs) and their smaller modular variants (SMRs) are part of the ‘Generation IV International Forum’ (GIF) on advanced nuclear energy systems. These reactors operate beyond the critical point of water (tc = 373.95 °C and P [...] Read more.
(1) Background: Supercritical water-cooled reactors (SCWRs) and their smaller modular variants (SMRs) are part of the ‘Generation IV International Forum’ (GIF) on advanced nuclear energy systems. These reactors operate beyond the critical point of water (tc = 373.95 °C and Pc = 22.06 MPa), which introduces specific technical challenges that need to be addressed. The primary concerns involve the effects of intense radiation fields—including fast neutrons, recoil protons/oxygen ions, and γ rays—on the chemistry of the coolant fluid and the integrity of construction materials. (2) Methods: This study employs Monte Carlo simulations of radiation track chemistry to investigate the yields of radiolytic species in SCWRs/SMRs exposed to 2 MeV neutrons. In our calculations, only the contributions from the first three recoil protons with initial energies of 1.264, 0.465, and 0.171 MeV were considered. Our analysis was conducted at both subcritical (300 and 350 °C) and supercritical temperatures (400–600 °C), maintaining a constant pressure of 25 MPa. (3) Results: Our simulations provide insights into the radiolytic formation of chemical species such as eaq, H, H2, OH, and H2O2 from ~1 ps to 1 ms. Compared to data from radiation with low linear energy transfer (LET), the G(eaq) and G(OH) values obtained for fast neutrons show a similar temporal dependence but with smaller amplitude—a result demonstrating the high LET nature of fast neutrons. A notable outcome of our simulations is the marked increase in G(OH) and G(H2), coupled with a corresponding reduction in G(H), observed during the homogeneous chemical stage of radiolysis. This evolution is attributed to the oxidation of water by the H atom according to the reaction H + H2O → OH + H2. This reaction acts as a significant source of H2, potentially reducing the need to add extra hydrogen to the reactor’s coolant water to suppress the net radiolytic production of oxidizing species. Unlike in subcritical water, our simulations also indicate that G(H2O2) remains very low in low-density SCW throughout the interval from ~1 ps to 1 ms, suggesting that H2O2 is less likely to contribute to oxidative stress under these conditions. (4) Conclusions: The results of this study could significantly impact water-chemistry management in the proposed SCWRs and SCW-SMRs, which is crucial for assessing and mitigating the corrosion risks to reactor materials, especially for long-term operation. Full article
(This article belongs to the Section Chemical and Molecular Sciences)
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<p>The SRIM simulation of 1.264, 0.465, and 0.171 MeV recoil protons penetrating SCW at 400 °C and 25 MPa reveals total track lengths (or penetration depths) of ~230, 50.5, and 14.1 μm, respectively. These values were validated by our own Monte Carlo track structure simulations. A significant factor contributing to the observed straggling is the change in the charge state of the protons, due to electron capture and loss, as they move through the water. A total of 100 protons were simulated.</p>
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<p>Time evolution of yields for radiolytic species (e<sup>−</sup><sub>aq</sub>, H<sup>●</sup>, H<sub>2</sub>, <sup>●</sup>OH, and H<sub>2</sub>O<sub>2</sub>) formed during the radiolysis of pure, de-aerated water by 2 MeV neutrons at 300 °C (<b>a</b>), 350 °C (<b>b</b>), 400 °C (<b>c</b>), 500 °C (<b>d</b>), and 600 °C (<b>e</b>) at 25 MPa, calculated from our Monte Carlo track segment (recoil proton) yield simulations over the interval of 1 ps to 1 ms.</p>
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<p>Time evolution of <span class="html-italic">G</span>(e<sup>−</sup><sub>aq</sub>) (<b>a</b>), <span class="html-italic">G</span>(<sup>●</sup>OH) (<b>b</b>), <span class="html-italic">G</span>(H<sup>●</sup>) (<b>c</b>), <span class="html-italic">G</span>(H<sub>2</sub>) (<b>d</b>), and <span class="html-italic">G</span>(H<sub>2</sub>O<sub>2</sub>) (<b>e</b>) during the radiolysis of pure, de-aerated water by 2 MeV neutrons at temperatures of 300 (green lines), 350 (orange lines), 400 (black lines), 500 (red lines), and 600 (blue lines) °C at 25 MPa. These calculations are derived from our Monte Carlo track segment (recoil proton) yield simulations over the interval of 1 ps to 1 ms. The symbols represent experimental data; they are color-coded for clarity to match the curves with which they are associated: (<span style="color:#92D050">!</span><span style="color:#92D050">, green</span>) Elliot [<a href="#B30-applsci-14-07024" class="html-bibr">30</a>], <span style="color:#92D050">(</span><span style="color:#92D050">,</span><span style="color:#92D050">, green) </span>Elliot et al. [<a href="#B47-applsci-14-07024" class="html-bibr">47</a>], <span style="color:#92D050">(</span><span style="color:#92D050">7</span><span style="color:#92D050">, green) </span>Christensen [<a href="#B48-applsci-14-07024" class="html-bibr">48</a>] (recommended mean <span class="html-italic">G</span> values at ~280–300 °C. According to the author, these values are likely accurate within ~25%), and <span style="color:#FFC000">(</span><span style="color:#FFC000">B</span><span style="color:#FFC000">, orange) </span>Elliot and Bartels [<a href="#B13-applsci-14-07024" class="html-bibr">13</a>]. The symbol <span style="color:red">(</span><span style="color:red">Λ</span><span style="color:red">, red) </span>in Panel (<b>a</b>) represents Edwards’ <span class="html-italic">G</span>(e<sup>−</sup><sub>aq</sub>) value of 0.59 molecule/100 eV at 400 °C and 24.8 MPa [<a href="#B49-applsci-14-07024" class="html-bibr">49</a>], positioned at an assumed measurement time of ~3 μs [<a href="#B50-applsci-14-07024" class="html-bibr">50</a>,<a href="#B51-applsci-14-07024" class="html-bibr">51</a>]. Note that all the experimental data at 300 and 350 °C are positioned at the end of the spur/track expansion times, specifically within the range of ~40 to 100 ns [<a href="#B52-applsci-14-07024" class="html-bibr">52</a>]. To our knowledge, no experimental yield values for fast neutrons at 500 and 600 °C have been reported to date.</p>
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<p>Time-dependent extents Δ<span class="html-italic">G</span>(H<sub>2</sub>), expressed in molecules per 100 eV, of the main reactions contributing to the generation and decay of H<sub>2</sub> during the radiolysis of pure, de-aerated water by 2 MeV neutrons at 300 °C (<b>a</b>), 350 °C (<b>b</b>), 400 °C (<b>c</b>), 500 °C (<b>d</b>), and 600 °C (<b>e</b>) at 25 MPa, calculated from our Monte Carlo track segment (recoil proton) simulations over the interval of 1 ps to 1 ms. These outcomes indicate that the production of H<sub>2</sub> is largely driven by the oxidation of water by the H<sup>●</sup> atom at higher temperatures, particularly in SCW.</p>
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16 pages, 2498 KiB  
Article
Long-Term Effect of Crop Succession Systems on Soil Chemical and Physical Attributes and Soybean Yield
by Milla S. S. Alves, Natanael M. Nascimento, Luiz Antonio F. M. Pereira, Thiago A. Barbosa, Claudio Hideo Martins da Costa, Tiara M. Guimarães, Aracy Camilla T. P. Bezerra and Deivid L. Machado
Plants 2024, 13(16), 2217; https://doi.org/10.3390/plants13162217 (registering DOI) - 10 Aug 2024
Viewed by 212
Abstract
Most soybean producers in the Cerrado biome use the direct seeding system, making it essential to cultivate cash or cover crops in the off-season, to promote soil protection, as well as increase organic matter, which is directly related to improvements in the chemical [...] Read more.
Most soybean producers in the Cerrado biome use the direct seeding system, making it essential to cultivate cash or cover crops in the off-season, to promote soil protection, as well as increase organic matter, which is directly related to improvements in the chemical and physical characteristics of these soils. In this sense, this work was conducted in Jataí, state of Goias, Brazil, to evaluate the physical-chemical attributes of the soil and the performance of soybeans cultivated in different crop succession systems cultivated for 6 years in the region of Jataí, GO. The experimental design was randomized blocks with four plots and four replications; the crops that followed soybeans were arranged as follows: T1—corn (Zea mays); T2—pearl millet (Pennisetum glaucum); T3—Urochloa ruziziensis; and T4—corn + Urochloa ruziziensis. Soybean yield components and grain yield were evaluated in two harvests (2020/2021 and 2021/2022). Deformed and undisturbed soil samples were collected in 2022 to assess soil fertility and for physical analysis. The data were subjected to analysis of variance (F test) and the means were compared using the Tukey test at 5% probability. The soybean–millet succession system stood out for the chemical and physical attributes of the soil: calcium, magnesium, base saturation, hydrogen + aluminum, and total porosity. The crop succession system did not affect yield for the two years analyzed, but the accumulated grain yields were higher in the crop succession soybean/corn intercropped. The results highlight the importance of using cover crops in improving the physical and chemical qualities of the soil in the long term. However, in the Cerrado, there is a predominance of the soybean/corn succession system motivated by financial issues to the detriment of the qualitative aspects of the soil, in which the introduction of Urochloa ruziziensis in intercropping with corn would improve the chemical attributes of the soil and have a long-term impact on the accumulated grain production. Full article
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<p>Soil organic Matter (OM) soil acidity (pH), potential acidity (H  +  Al) and phosphor (P) in layers 0.0–0.05, 0.05–0.10, 0.10–0.20 and 0.20–0.40 m depth, after soybean growing season 2021/2022 in function of the crop-production systems. Jataí, GO. Horizontal bars indicate the least significant difference of Tukey test (<span class="html-italic">p</span> &lt; 0 .05) for each depth and “ns” indicates that the ANOVA was not significant.</p>
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<p>Potassium (K<sup>+</sup>), calcium (Ca<sup>2+</sup>), magnesium (Mg<sup>2+</sup>) and sum of bases (SB) in layers 0.0–0.05, 0.05–0.10, 0.10–0.20 and 0.20–0.40 m depth, after soybean growing season 2021/2022 as a function of the crop-production systems. Jataí, GO. Horizontal bars indicate the least significant difference of Tukey test (<span class="html-italic">p</span> &lt; 0.05) for each depth and “ns” indicates that the ANOVA was not significant.</p>
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<p>Cation exchange capacity (CEC) and base saturation (BS) in layers 0.0–0.05, 0.05–0.10, 0.10–0.20 and 0.20–0.40 m depth, after soybean growing season 2021/2022 in function of the crop-production systems. Jataí, GO. Horizontal bars indicate the least significant difference of Tukey test (<span class="html-italic">p</span> &lt; 0.05) for each depth.</p>
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<p>Bulk density (BK), particle density (PD), total porosity (TP) in layers 0.0–0.05, 0.05–0.10, 0.10–0.20 and 0.20–0.40 m depth, after soybean growing season 2021/2022 as a function of the crop-production systems. Jataí, GO. Horizontal bars indicate the least significant difference of Tukey test (<span class="html-italic">p</span> &lt; 0.05) for each depth and “ns” indicates that the ANOVA was not significant.</p>
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<p>Weighted mean diameter (WMD) in layer 0.0–0.20 m, after soybean growing season 2021/2022 as a function of the crop-production systems. Jataí, GO. Different letters represent significative difference between the treatments.</p>
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<p>Plant final population (POP) and Yield (Y) as a function of crop succession systems, averages for growing season 2020/2021 and 2021/2022. Jataí, GO. Different letters represent significative differences between the treatments.</p>
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<p>Schematic of crop succession systems and experiment timeline.</p>
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13 pages, 3856 KiB  
Article
Coupling Electro-Fenton and Electrocoagulation of Aluminum–Air Batteries for Enhanced Tetracycline Degradation: Improving Hydrogen Peroxide and Power Generation
by Zhenghan Zhou, Wei Wei, Houfan Wu, Haoyang Gong, Kai Zhou, Qiyuan Zheng, Shaogen Liu, Ling Gui, Zhongqi Jiang and Shuguang Zhu
Molecules 2024, 29(16), 3781; https://doi.org/10.3390/molecules29163781 (registering DOI) - 9 Aug 2024
Viewed by 360
Abstract
Electro-Fenton (EF) technology has shown great potential in environmental remediation. However, developing efficient heterogeneous EF catalysts and understanding the relevant reaction mechanisms for pollutant degradation remain challenging. We propose a new system that combines aluminum–air battery electrocoagulation (EC) with EF. The system utilizes [...] Read more.
Electro-Fenton (EF) technology has shown great potential in environmental remediation. However, developing efficient heterogeneous EF catalysts and understanding the relevant reaction mechanisms for pollutant degradation remain challenging. We propose a new system that combines aluminum–air battery electrocoagulation (EC) with EF. The system utilizes dual electron reduction of O2 to generate H2O2 in situ on the air cathodes of aluminum–air batteries and the formation of primary cells to produce electricity. Tetracycline (TC) is degraded by ·OH produced by the Fenton reaction. Under optimal conditions, the system exhibits excellent TC degradation efficiency and higher H2O2 production. The TC removal rate by the reaction system using a graphite cathode reached nearly 100% within 4 h, whereas the H2O2 yield reached 127.07 mg/L within 24 h. The experimental results show that the novel EF and EC composite system of aluminum–air batteries, through the electroflocculation mechanism and ·OH and EF reactions, with EC as the main factor, generates multiple •OH radicals that interact to efficiently remove TC. This work provides novel and important insights into EF technology, as well as new strategies for TC removal. Full article
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<p>SEM images of (<b>a</b>) AC, (<b>b</b>) CB, and (<b>c</b>) G cathodes at a magnification of 15 K.</p>
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<p>N<sub>2</sub> adsorption/desorption isotherms of different carbon–PTFE powders.</p>
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<p>Linear sweep voltammetry of three air electrodes.</p>
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<p>Power density and polarization curves of aluminum–air batteries using different cathodes: (<b>a</b>) AC, (<b>b</b>) CB, and (<b>c</b>) G cathodes.</p>
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<p>H<sub>2</sub>O<sub>2</sub> concentration of aluminum–air batteries using AC, CB, and G cathodes.</p>
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<p>TC removal rates for different NaCl concentrations (<b>a</b>), initial TC concentrations (<b>b</b>), Fe<sup>2+</sup> concentrations (<b>c</b>), and external resistance (<b>d</b>).</p>
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<p>(<b>a</b>) Current density; (<b>b</b>) H<sub>2</sub>O<sub>2</sub> production versus time of Al–air batteries at different external resistance levels.</p>
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<p>(<b>a</b>) Removal rate of TC in the different systems. (<b>b</b>) EPR spectrum of DMPO-⋅OH.</p>
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<p>Mechanism of TC pollutant degradation by the EF and EC composite system.</p>
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<p>UV–vis spectra during the degradation of TC in different systems.</p>
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44 pages, 1008 KiB  
Article
Exergy Analysis in Highly Hydrogen-Enriched Methane Fueled Spark-Ignition Engine at Diverse Equivalence Ratios via Two-Zone Quasi-Dimensional Modeling
by Dimitrios C. Rakopoulos, Constantine D. Rakopoulos, George M. Kosmadakis, Evangelos G. Giakoumis and Dimitrios C. Kyritsis
Energies 2024, 17(16), 3964; https://doi.org/10.3390/en17163964 (registering DOI) - 9 Aug 2024
Viewed by 267
Abstract
In the endeavor to accomplish a fully de-carbonized globe, sparkling interest is growing towards using natural gas (NG) having as vastly major component methane (CH4). This has the lowest carbon/hydrogen atom ratio compared to other conventional fossil fuels used in engines [...] Read more.
In the endeavor to accomplish a fully de-carbonized globe, sparkling interest is growing towards using natural gas (NG) having as vastly major component methane (CH4). This has the lowest carbon/hydrogen atom ratio compared to other conventional fossil fuels used in engines and power-plants hence mitigating carbon dioxide (CO2) emissions. Given that using neat hydrogen (H2) containing nil carbon still possesses several issues, blending CH4 with H2 constitutes a stepping-stone towards the ultimate goal of zero producing CO2. In this context, the current work investigates the exergy terms development in high-speed spark-ignition engine (SI) fueled with various hydrogen/methane blends from neat CH4 to 50% vol. fraction H2, at equivalence ratios (EQR) from stoichiometric into the lean region. Experimental data available for that engine were used for validation from the first-law (energy) perspective plus emissions and cycle-by-cycle variations (CCV), using in-house, comprehensive, two-zone (unburned and burned), quasi-dimensional turbulent combustion model tracking tightly the flame-front pathway, developed and reported recently by authors. The latter is expanded to comprise exergy terms accompanying the energy outcomes, affording extra valuable information on judicious energy usage. The development in each zone, over the engine cycle, of various exergy terms accounting too for the reactive and diffusion components making up the chemical exergy is calculated and assessed. The correct calculation of species and temperature histories inside the burned zone subsequent to entrainment of fresh mixture from the unburned zone contributes to more exact computation, especially considering the H2 percentage in the fuel blend modifying temperature-levels, which is key factor when the irreversibility is calculated from a balance comprising all rest exergy terms. Illustrative diagrams of the exergy terms in every zone and whole charge reveal the influence of H2 and EQR values on exergy terms, furnishing thorough information. Concerning the joint content of both zones normalized exergy values over the engine cycle, the heat loss transfer exergy curves acquire higher values the higher the H2 or EQR, the work transfer exergy curves acquire slightly higher values the higher the H2 and slightly higher values the lower the EQR, and the irreversibility curves acquire lower values the higher the H2 or EQR. This exergy approach can offer new reflection for the prospective research to advancing engines performance along judicious use of fully friendly ecological fuel as H2. This extended and in-depth exergy analysis on the use of hydrogen in engines has not appeared in the literature. It can lead to undertaking corrective actions for the irreversibility, exergy losses, and chemical exergy, eventually increasing the knowledge of the SI engines science and technology for building smarter control devices when fueling the IC engines with H2 fuel, which can prove to be game changer to attaining a clean energy environment transition. Full article
(This article belongs to the Special Issue Internal Combustion Engine Performance 2024)
52 pages, 8354 KiB  
Review
A Comprehensive Study on Hydrogen Production via Waste Heat Recovery of a Natural Gas-Fueled Internal Combustion Engine in Cogeneration Power-Hydrogen Layouts: 4E Study and Optimization
by Mohammad Zoghi, Nasser Hosseinzadeh, Saleh Gharaie and Ali Zare
Sustainability 2024, 16(16), 6860; https://doi.org/10.3390/su16166860 (registering DOI) - 9 Aug 2024
Viewed by 221
Abstract
Internal combustion engines (ICEs) are one of the significant sources of wasted energy, with approximately 65% of their input energy being wasted and dissipated into the environment. Given their wide usage globally, it is necessary to find ways to recover their waste energies, [...] Read more.
Internal combustion engines (ICEs) are one of the significant sources of wasted energy, with approximately 65% of their input energy being wasted and dissipated into the environment. Given their wide usage globally, it is necessary to find ways to recover their waste energies, addressing this inefficiency and reducing environmental pollution. While previous studies have explored various aspects of waste energy recovery, a comparative analysis of different bottoming configurations has been lacking. In this research, an extensive review of the existing literature was conducted by an exploration of four key bottoming cycles: the steam Rankine cycle (SRC), CO2 supercritical Brayton cycle, inverse Brayton cycle (IBC), and air bottoming cycle. In addition, these four main bottoming systems are utilized for the waste energy recovery of natural gas-fired ICE with a capacity of 584 kW and an exhausted gas temperature of 493 °C. For the efficient waste heat recovery of residual exhausted gas and heat rejection stage of the main bottoming system, two thermoelectric generators are utilized. Then, the produced power in bottoming systems is sent to a proton exchange membrane electrolyzer for hydrogen production. A comprehensive 4E (energy, exergy, exergy-economic, and environmental) optimization is conducted to find the best main bottoming system for hydrogen production. Results showed that the SRC-based system has the highest exergy efficiency (21.93%), while the IBC-based system results in the lowest efficiency (13.72%), total cost rate (25.58 $/h), and unit cost of hydrogen production (59.91 $/GJ). This combined literature review and research article underscore the importance of finding an economically efficient bottoming cycle in the context of waste energy recovery and hydrogen production. Full article
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<p>Configuration 1: SRC-based combined hydrogen production system.</p>
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<p>Configuration 2: SBC-based combined hydrogen production system.</p>
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<p>Configuration 3: IBC-based combined hydrogen production system.</p>
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<p>Configuration 4: ABC-based combined hydrogen production system.</p>
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<p>PEME’s cell potential–current density in comparison with [<a href="#B116-sustainability-16-06860" class="html-bibr">116</a>].</p>
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<p>The flow chart of simulation and optimization.</p>
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<p>The effect of T<sub>HRSG,SRC</sub> on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of pinch point temperature difference on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of HRSG superheating temperature on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of T<sub>con</sub> on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of T<sub>in,com</sub> on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of P<sub>in,com</sub> on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of PR<sub>com</sub> on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of hot side temperature difference of HRHX on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of IBTBP on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of T<sub>in,com,IBC</sub> on the output parameters.(<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of PR<sub>com.ABC</sub> on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The effect of hot side temperature difference of AHX on the output parameters. (<b>a</b>) On exergy efficiency and total exergy destruction; (<b>b</b>) on total cost rate and unit cost of product.</p>
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<p>The SRC-based system’s Pareto front diagram as a result (Configuration 1).</p>
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<p>The SBC-based system’s Pareto front diagram as a result (Configuration 1).</p>
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<p>The IBC-based system’s Pareto front diagram as a result (Configuration 1).</p>
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<p>The ABC-based system’s Pareto front diagram as a result (Configuration 1).</p>
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