Nothing Special   »   [go: up one dir, main page]

You seem to have javascript disabled. Please note that many of the page functionalities won't work as expected without javascript enabled.
 
 
Sign in to use this feature.

Years

Between: -

Subjects

remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline

Journals

remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline

Article Types

Countries / Regions

remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline
remove_circle_outline

Search Results (471)

Search Parameters:
Keywords = microwave plasma

Order results
Result details
Results per page
Select all
Export citation of selected articles as:
40 pages, 12596 KiB  
Review
A Review on the Additive Manufacturing of W-Cu Composites
by Muhammad Hussain, Bosheng Dong, Zhijun Qiu, Ulf Garbe, Zengxi Pan and Huijun Li
Metals 2025, 15(2), 197; https://doi.org/10.3390/met15020197 - 13 Feb 2025
Abstract
In recent years, W-Cu composite systems have become very interesting subjects due to good electrical and thermal conductivity, high-temperature strength, certain plasticity, and excellent radiation resistance. W-Cu composites are a very important class of materials in applications like PFM (plasma facing materials), functional [...] Read more.
In recent years, W-Cu composite systems have become very interesting subjects due to good electrical and thermal conductivity, high-temperature strength, certain plasticity, and excellent radiation resistance. W-Cu composites are a very important class of materials in applications like PFM (plasma facing materials), functional graded materials (FGM), electronic packaging materials, high-voltage electrical contacts, sweating materials, shaped charge liners, electromagnetic gun-rail materials, kinetic energy penetrators, and radiation shielding/protection. There is no possibility of forming a crystalline structure between these two materials. However, due to the unique properties these materials possess, they can be used by preparing them as a composite. Generally, W-Cu composites are prepared via the conventional powder metallurgy routes, i.e., sintering, hot pressing, hot isostatic pressing, isostatic cold pressing, sintering and infiltration, and microwave sintering. However, these processes have certain limitations, like the inability to produce bulk material, they are expensive, and their adoptability is limited. Here, in this review, we will discuss in detail the fabrication routes of additive manufacturing, and its current progress, challenges, trends, and associated properties obtained. We will also explain the challenges for the additive manufacturing of the composite. We will also compare W-Cu composites to other materials that can challenge them in terms of specific applications or service conditions. The solidification mechanism will be explained for W-Cu composites in additive manufacturing. Finally, we will conclude the progress of additive manufacturing of W-Cu composites to date and suggest future recommendations based on the current challenges in additive manufacturing. Full article
(This article belongs to the Section Welding and Joining)
Show Figures

Figure 1

Figure 1
<p>Phase diagram of W and Cu. Reprinted with permission from Ref. [<a href="#B45-metals-15-00197" class="html-bibr">45</a>].</p>
Full article ">Figure 2
<p>Gibbs free energy vs. alloy composition, Reprinted with permission from Ref. [<a href="#B46-metals-15-00197" class="html-bibr">46</a>]. 1985, AIP Publishing.</p>
Full article ">Figure 3
<p>Formation enthalpy calculated vs. compositional ratios using MD simulations, reprinted with permission from ref. [<a href="#B48-metals-15-00197" class="html-bibr">48</a>], 2017, Elsevier.</p>
Full article ">Figure 4
<p>Surface energy of different materials studied in the research, reprinted from [<a href="#B49-metals-15-00197" class="html-bibr">49</a>].</p>
Full article ">Figure 5
<p>Surface energy of different transition metals and W (The dotted line shows results based on FCD-LMTO calculations), reprinted with permission from ref. [<a href="#B50-metals-15-00197" class="html-bibr">50</a>], 2018, Elsevier.</p>
Full article ">Figure 6
<p>Effect of nano-sized particles on the formation enthalpy for W50Cu50 system, reprinted from Ref. [<a href="#B47-metals-15-00197" class="html-bibr">47</a>].</p>
Full article ">Figure 7
<p>(<b>a</b>) Discontinuous FGM and (<b>b</b>) continuous FGM, (<b>c</b>–<b>e</b>) schematic diagrams showing discontinuous FGMs that contain interfaces with gradual change in composition, grain orientation and volume fractions of two types of second-phase particles, respectively. (<b>f</b>–<b>h</b>) schematic diagrams showing continuous FGMs in absence of interfaces and with gradual change in grain size, fiber orientation and volume fraction of second-phase particles. Reprinted with permission from Ref. [<a href="#B62-metals-15-00197" class="html-bibr">62</a>], 2019, Elsevier.</p>
Full article ">Figure 8
<p>Shift (red arrow) in Ductile-to-brittle transition temperature (DBTT) of W tested in cold-rolled, hot-rolled, and annealed conditions in LS and TS orientations. Reprinted with permission from Ref. [<a href="#B65-metals-15-00197" class="html-bibr">65</a>], 2016, Elsevier.</p>
Full article ">Figure 9
<p>Effect of Re addition on DBTT in W, reprinted with permission from Ref. [<a href="#B66-metals-15-00197" class="html-bibr">66</a>], 2018, Elsevier.</p>
Full article ">Figure 10
<p>Mechanistic models of heat and mass transfer and fluid flow in AM. reprinted with permission from Ref. [<a href="#B70-metals-15-00197" class="html-bibr">70</a>].</p>
Full article ">Figure 11
<p>(<b>a</b>) Infiltration method for W-Cu production. (<b>b</b>) W-Cu microstructure obtained, reprinted with permission from Ref. [<a href="#B25-metals-15-00197" class="html-bibr">25</a>], 2018, Elsevier.</p>
Full article ">Figure 12
<p>Liquid-phase sintering mechanism, reprinted with permission from Ref. [<a href="#B78-metals-15-00197" class="html-bibr">78</a>], 2009, Springer Nature.</p>
Full article ">Figure 13
<p>(<b>a</b>) Vacuum and (<b>b</b>) microwave heating (the intensity of color represents the heat energy), reprinted with permission from Ref. [<a href="#B82-metals-15-00197" class="html-bibr">82</a>], 2024, Wiley.</p>
Full article ">Figure 14
<p>Schematic of hot-pressing process, reprinted with permission from Ref. [<a href="#B60-metals-15-00197" class="html-bibr">60</a>], 2008, Elsevier.</p>
Full article ">Figure 15
<p>Spark plasma sintering setup and the heating mechanism, reprinted with permission from Ref. [<a href="#B82-metals-15-00197" class="html-bibr">82</a>], 2024, Wiley.</p>
Full article ">Figure 16
<p>Schematic of injection molding, reprinted with permission from Ref. [<a href="#B25-metals-15-00197" class="html-bibr">25</a>], 2018, Elsevier.</p>
Full article ">Figure 17
<p>Schematic of mechanical alloying: (<b>a</b>) process and (<b>b</b>) mechanism. Reprinted with permission from Ref. [<a href="#B92-metals-15-00197" class="html-bibr">92</a>], 2013, Elsevier.</p>
Full article ">Figure 18
<p>A schematic of fabrication of W-Cu composite using laser technology, reprinted with permission from Ref. [<a href="#B93-metals-15-00197" class="html-bibr">93</a>], 2020, Elsevier.</p>
Full article ">Figure 19
<p>W-Cu composite prepared by laser additive manufacturing technology with different scanning and laser-power levels, reprinted with permission from Ref. [<a href="#B94-metals-15-00197" class="html-bibr">94</a>], 2018, Elsevier.</p>
Full article ">Figure 20
<p>Schematic of electron beam melting, reprinted from Ref. [<a href="#B96-metals-15-00197" class="html-bibr">96</a>].</p>
Full article ">Figure 21
<p>SEM surface morphology of the W-(Ni)-Cu composites. (<b>a</b>) W-Cu40 wt.%; (<b>b</b>) W-Cu30 wt.%; (<b>c</b>) W-Cu25 wt.%; and (<b>d</b>) W-Ni5 wt.%–Cu15 wt.%, reprinted with permission from Ref. [<a href="#B42-metals-15-00197" class="html-bibr">42</a>], 2016, Elsevier.</p>
Full article ">Figure 22
<p>Surface SEM images of Cu-15W sample before and after HCPEB irradiation. (<b>a</b>) Initial, (<b>b</b>) 5 pulses, (<b>c</b>) 10 pulses, and (<b>d</b>) BSE image of 10-pulsed sample, reprinted with permission from Ref. [<a href="#B43-metals-15-00197" class="html-bibr">43</a>], 2018, Elsevier.</p>
Full article ">Figure 23
<p>Cross-sections of three-layer W–Cu cladding on a steel substrate: (<b>a</b>) one layer (75% W), (<b>b</b>) two layers (75% + 95% W), and (<b>c</b>) three layers (75% + 95% + 98% W), reprinted from Ref. [<a href="#B44-metals-15-00197" class="html-bibr">44</a>].</p>
Full article ">Figure 24
<p>Typical (<b>a</b>,<b>b</b>) microstructure and (<b>c</b>) XRD of W and Cu system, reprinted with permission from Ref. [<a href="#B19-metals-15-00197" class="html-bibr">19</a>], 2022, Elsevier.</p>
Full article ">Figure 25
<p>TEM observations at W/Cu interface: (<b>a</b>) HAADF image; (<b>b</b>) EDX line-scanning profile along the red arrow marked in (<b>a</b>); (<b>c</b>,<b>d</b>) element mapping; (<b>e</b>) HAADF image of the W/Cu interface; and (<b>f</b>) HR-TEM image of the interface, reprinted with permission from Ref. [<a href="#B151-metals-15-00197" class="html-bibr">151</a>], 2022, Elsevier.</p>
Full article ">Figure 26
<p>Colling rate on (<b>a</b>) Cu substrate; and (<b>b</b>) Cu, Al, and SS substrate, reprinted with permission from Ref. [<a href="#B172-metals-15-00197" class="html-bibr">172</a>], 1995, Elsevier.</p>
Full article ">Figure 27
<p>Schematic of laser welding and molten pool formation, reprinted from Ref. [<a href="#B178-metals-15-00197" class="html-bibr">178</a>].</p>
Full article ">Figure 28
<p>Schematic of electron beam melting, reprinted with permission from Ref. [<a href="#B179-metals-15-00197" class="html-bibr">179</a>], 2016, Elsevier.</p>
Full article ">Figure 29
<p>(<b>a</b>) Schematic of the welding principle, (<b>b</b>) Material states, fluid flow and four types of forces involved during the welding process, reprinted from Ref. [<a href="#B181-metals-15-00197" class="html-bibr">181</a>].</p>
Full article ">Figure 30
<p>The degree of undercooling explained (<b>a</b>) Hypocooling, (<b>b</b>) Critical undercooling, (<b>c</b>) Hypercooling, reprinted with permission from Ref. [<a href="#B185-metals-15-00197" class="html-bibr">185</a>], 2010, Springer.</p>
Full article ">Figure 31
<p>Geometrically necessary dislocations (GNDs) and statistically stored dislocations (SSDs), reprinted with permission from Ref. [<a href="#B187-metals-15-00197" class="html-bibr">187</a>], 2019, Elsevier.</p>
Full article ">Figure 32
<p>Solidification mechanism of W-Cu system explained in four steps, reprinted with permission from Ref. [<a href="#B19-metals-15-00197" class="html-bibr">19</a>], 2022, Elsevier.</p>
Full article ">
39 pages, 5294 KiB  
Review
Large Scale Synthesis of Carbon Dots and Their Applications: A Review
by Zhujun Huang and Lili Ren
Molecules 2025, 30(4), 774; https://doi.org/10.3390/molecules30040774 - 7 Feb 2025
Abstract
Carbon dots (CDs), a versatile class of fluorescent carbon-based nanomaterials, have attracted widespread attention due to their exceptional optical properties, biocompatibility, and cost-effectiveness. Their applications span biomedicine, optoelectronics, and smart food packaging, yet large-scale synthesis remains a significant challenge. This review categorizes large-scale [...] Read more.
Carbon dots (CDs), a versatile class of fluorescent carbon-based nanomaterials, have attracted widespread attention due to their exceptional optical properties, biocompatibility, and cost-effectiveness. Their applications span biomedicine, optoelectronics, and smart food packaging, yet large-scale synthesis remains a significant challenge. This review categorizes large-scale synthesis methods into liquid-phase (hydrothermal/solvothermal, microwave-assisted, magnetic hyperthermia, aldol condensation polymerization), gas-phase (plasma synthesis), solid-phase (pyrolysis, oxidation/carbonization, ball milling), and emerging techniques (microfluidic, ultrasonic, molten-salt). Notably, microwave-assisted and solid-state synthesis methods show promise for industrial production due to their scalability and efficiency. Despite these advances, challenges persist in optimizing synthesis reproducibility, reducing energy consumption, and developing purification methods and quality control strategies. Addressing these issues will be critical for transitioning CDs from laboratory research to real-world applications. Full article
(This article belongs to the Section Nanochemistry)
Show Figures

Figure 1

Figure 1
<p>Outline of synthesis and application of CDs.</p>
Full article ">Figure 2
<p>(<b>a</b>) Schematic illustration of preparation of SW-CPDs [<a href="#B62-molecules-30-00774" class="html-bibr">62</a>]; (<b>b</b>) Photographs showing RTP behavior of SW-CPDs under 365 nm UV light [<a href="#B62-molecules-30-00774" class="html-bibr">62</a>]; (<b>c</b>) SW-CPDs obtained in a single reaction with weight exceeding 10 g [<a href="#B62-molecules-30-00774" class="html-bibr">62</a>]; (<b>d</b>) Schematic illustration of preparation of URTP CDs [<a href="#B64-molecules-30-00774" class="html-bibr">64</a>]; (<b>e</b>) Photographs showing RTP behavior of URTP CDs under 365 nm UV light for CD-250, CD-300, CD-400 and CD-500 [<a href="#B64-molecules-30-00774" class="html-bibr">64</a>]; (<b>f</b>) Photograph of CD-400 in large-scale synthesis [<a href="#B64-molecules-30-00774" class="html-bibr">64</a>].</p>
Full article ">Figure 3
<p>(<b>a</b>) Photograph of industrial-level apparatus (50 L stainless steel autoclave) [<a href="#B71-molecules-30-00774" class="html-bibr">71</a>]; (<b>b</b>) Photograph of concentrated aqueous dispersions (20 L) of GQDs available on an industrial scale, dried powder (100 g) and a diluted dispersion under a UV light [<a href="#B71-molecules-30-00774" class="html-bibr">71</a>]; (<b>c</b>) Schematic illustration of preparation of BNP-CDs by utilizing various crosslinking agents and heteroatoms co-doping [<a href="#B75-molecules-30-00774" class="html-bibr">75</a>]; (<b>d</b>) Schematic illustration of synthesis of CDs from poplar leaves [<a href="#B78-molecules-30-00774" class="html-bibr">78</a>]; (<b>e</b>) Schematic illustration of hydrothermal synthesis process of CDs, followed by alkaline treatment. The original labels (<b>a</b>–<b>e</b>) correspond to different stages in the referenced study [<a href="#B79-molecules-30-00774" class="html-bibr">79</a>]; (<b>f</b>) Schematic illustration of preparation of N-CDs from sodium alginate [<a href="#B80-molecules-30-00774" class="html-bibr">80</a>].</p>
Full article ">Figure 4
<p>(<b>a</b>) Schematic illustration of preparation of CDs by microwave-assisted carbonization of surfactants [<a href="#B98-molecules-30-00774" class="html-bibr">98</a>]; (<b>b</b>) Illustration for the Synthesis of TTDDA-Based CQDs from CA and TTDDA [<a href="#B87-molecules-30-00774" class="html-bibr">87</a>]; (<b>c</b>) Synthesis mechanism elucidation of CDs and their applications [<a href="#B91-molecules-30-00774" class="html-bibr">91</a>]; (<b>d</b>) Schematic illustration of kilogram-scale synthesis of full-color solid-state fluorescent CDs [<a href="#B92-molecules-30-00774" class="html-bibr">92</a>].</p>
Full article ">Figure 5
<p>(<b>a</b>) Synthesis scheme for multi-color CDs [<a href="#B122-molecules-30-00774" class="html-bibr">122</a>]; (<b>b</b>) Schematic diagram showing the proposed formation process of CDs [<a href="#B125-molecules-30-00774" class="html-bibr">125</a>]; (<b>c</b>) Photographs of each step in the preparation of CDs [<a href="#B125-molecules-30-00774" class="html-bibr">125</a>].</p>
Full article ">Figure 6
<p>(<b>a</b>) Selective fluorescence imaging of Gram-positive bacteria using CDs [<a href="#B154-molecules-30-00774" class="html-bibr">154</a>]; (<b>b</b>) Schematic diagram of CDs preparation and applications [<a href="#B155-molecules-30-00774" class="html-bibr">155</a>]; (<b>c</b>) Schematic illustration of the Mn-CD assembly to enhance the anticancer efficiency of PDT [<a href="#B162-molecules-30-00774" class="html-bibr">162</a>]; (<b>d</b>) In vivo and ex vivo FL images of tumors at different time [<a href="#B162-molecules-30-00774" class="html-bibr">162</a>].</p>
Full article ">Figure 7
<p>(<b>a</b>) The PL spectra versus different Cu<sup>2+</sup> and Hg<sup>2+</sup> concentrations. The insets are digital images with and without Cu<sup>2+</sup>/Hg<sup>2+</sup> addition [<a href="#B132-molecules-30-00774" class="html-bibr">132</a>]; (<b>b</b>) The PL spectra of N-CQD and S-CQD systems [<a href="#B132-molecules-30-00774" class="html-bibr">132</a>].</p>
Full article ">Figure 8
<p>(<b>a</b>) Schematic illustration of preparation of three colors CDs [<a href="#B16-molecules-30-00774" class="html-bibr">16</a>]; (<b>b</b>) Photoluminescence photographs of m-CDs, o-CDs, p-CDs, and their mixtures in PVA composite films UV irradiation [<a href="#B16-molecules-30-00774" class="html-bibr">16</a>]; (<b>c</b>) Synthetic strategy of full-color fluorescent CDs [<a href="#B181-molecules-30-00774" class="html-bibr">181</a>].</p>
Full article ">Figure 9
<p>(<b>a</b>) Photograph of tangerines’ and strawberries’ appearance change [<a href="#B188-molecules-30-00774" class="html-bibr">188</a>]; (<b>b</b>) Photograph of bananas on different days [<a href="#B193-molecules-30-00774" class="html-bibr">193</a>].</p>
Full article ">
16 pages, 5450 KiB  
Article
A Unique Dual-Shell Structure with Highly Active Ni@SiC/CNT/CNF Microwave Catalysts
by Xizong Liu, Yulei Zhang, Heng Wu, Dongsheng Zhang, Jiaqi Liu and Haibo Ouyang
Catalysts 2025, 15(2), 132; https://doi.org/10.3390/catal15020132 - 30 Jan 2025
Abstract
Microwave-assisted catalytic oxidation (MACO) is a novel wastewater treatment technology for the efficient treatment degradation of organic wastewater. However, a single carbon material or SiC has limited absorption of electromagnetic waves, and the efficiency of using it as a microwave-assisted organic catalyst is [...] Read more.
Microwave-assisted catalytic oxidation (MACO) is a novel wastewater treatment technology for the efficient treatment degradation of organic wastewater. However, a single carbon material or SiC has limited absorption of electromagnetic waves, and the efficiency of using it as a microwave-assisted organic catalyst is not satisfactory. To improve the absorption and microwave-assisted degradation performance of carbon matrix composites, a new carbon magnetic composite Ni@SiC/CNT/CNF microwave catalyst is constructed. By controlling the introduction of nickel, different numbers of carbon nanotubes are grown on the surface of carbon nanofibers, and C and SiC double-shell structures were formed on the top of the carbon nanotubes, which catalyzed the generation of active groups by the thermal effect generated by the plasma discharge under the action of microwave field, thus realizing the highly efficient catalytic degradation of wastewater dyes. The results show that the Ni@SiC/CNT/CNF with the lowest reflection loss of RLmin = −9.26 dB exhibit excellent degradation capabilities with a degradation efficiency of 99.9% for methylene blue within 90 s under 450 W microwave irradiation. Full article
Show Figures

Figure 1

Figure 1
<p>(<b>a</b>) XRD patterns; (<b>b</b>) Raman spectra; and (<b>c</b>) I<sub>D</sub>/I<sub>G</sub> histogram.</p>
Full article ">Figure 2
<p>(<b>a</b>) XPS full spectrum and (<b>b</b>) XPS high-resolution spectrum of C 1s, (<b>c</b>) Si 2p, and (<b>d</b>) Ni 2p for the NSCT15 composites.</p>
Full article ">Figure 3
<p>(<b>a</b>–<b>c</b>) SEM images of NSCT15 composites and (<b>d</b>–<b>f</b>) SEM images of NSCT30.</p>
Full article ">Figure 4
<p>TEM images of the NSCT30: (<b>a</b>,<b>b</b>) low magnification; (<b>c</b>) HR-TEM images; (<b>d</b>,<b>e</b>) individual nickel particle point energy spectra.</p>
Full article ">Figure 5
<p>Formation mechanism of the SiC interface layer of composite materials.</p>
Full article ">Figure 6
<p>(<b>a</b>) UV absorption spectra of NSCT30 composites for MB and (<b>b</b>) UV absorption spectra of NSCT15 (d 30 min means the 30-min dark reaction).</p>
Full article ">Figure 7
<p>Plasma discharge phenomena of composite materials under microwave catalysis: (<b>a</b>) NSCT15 and (<b>b</b>) NSCT30.</p>
Full article ">Figure 8
<p>(<b>a</b>) Degradation curves of composites for MB under microwave radiation; (<b>b</b>) first-order kinetic curve; (<b>c</b>) the corresponding degradation slopes and their R<sup>2</sup>.</p>
Full article ">Figure 9
<p>Complex permittivity, permeability, and tanδ curves of NSCT composites: (<b>a</b>) ε′; (<b>b</b>) ε″; (<b>c</b>) tanδ<sub>ε</sub>; (<b>d</b>) μ′; (<b>e</b>) μ″; (<b>f</b>) tanδ<sub>μ</sub>.</p>
Full article ">Figure 10
<p>Typical Cole–Cole semicircles for (<b>a</b>) NSCT15 and (<b>b</b>) NSCT30.</p>
Full article ">Figure 11
<p>Reflection loss (RL) curves for NSCT composites.</p>
Full article ">Figure 12
<p>Degradation mechanism of methylene blue by Ni@SiC/CNTs/CNFs under microwave irradiation.</p>
Full article ">Figure 13
<p>Process flow diagram of Ni@SiC/CNT/CNF composites.</p>
Full article ">
15 pages, 6215 KiB  
Article
Ultrasound-Assisted Determination of Selenium in Organic Rice Using Deep Eutectic Solvents Coupled with Inductively Coupled Plasma Mass Spectrometry
by Shanshan Zhang, Boyu Chen, Yu Liu, Haoyu Sun, Haixing Zhang, Na Li, Yang Qing, Jeevithan Elango, Dayun Zhao and Wenhui Wu
Foods 2025, 14(3), 384; https://doi.org/10.3390/foods14030384 - 24 Jan 2025
Viewed by 280
Abstract
As the focus on green chemistry intensifies, researchers are progressively looking to incorporate biodegradable and environmentally friendly solvents. Given the prevalent use of inorganic solvents in conventional methods for detecting selenium content, this study utilized a mixture design approach to create four deep [...] Read more.
As the focus on green chemistry intensifies, researchers are progressively looking to incorporate biodegradable and environmentally friendly solvents. Given the prevalent use of inorganic solvents in conventional methods for detecting selenium content, this study utilized a mixture design approach to create four deep eutectic solvents (DESs). The elements of the DESs consisted of six different compounds: guanidine hydrochloride, fructose, glycerol, citric acid, proline, and choline chloride. The synthesized deep eutectic solvents (DESs) exhibited a uniform and transparent appearance. The ideal ratios for each DES were established based on their density and viscosity measurements, leading to the formulations of DES1 (34% guanidine hydrochloride, 21% fructose, 45% water), DES2 (23% guanidine hydrochloride, 32% glycerol, 45% water), DES3 (27.5% citric acid, 27.5% proline, 45% water), and DES4 (30% choline chloride, 25% citric acid, 45% water). The characterization of the deep eutectic solvents (DESs) was performed using nuclear magnetic resonance (NMR) spectroscopy and infrared (IR) spectroscopy, which confirmed the molecular formation of each DES. Following this, the DESs were applied as extraction solvents in a process involving ultrasonic-assisted microextraction (UAE) combined with inductively coupled plasma mass spectrometry (ICP-MS) to assess the selenium levels in selenium-rich rice. The results were benchmarked against traditional microwave-assisted acid digestion (TM-AD), revealing selenium recovery rates ranging from 85.5% to 106.7%. These results indicate that UAE is an effective method for extracting selenium from selenium-rich rice, thereby establishing a solid data foundation for the environmentally friendly analysis of selenium content in rice. Full article
(This article belongs to the Section Food Analytical Methods)
Show Figures

Figure 1

Figure 1
<p>Constrained mixture design for the synthesis of 4 different DESs. DES1: guanidine hydrochloride (component 1), fructose (component 2), and water; DES2: guanidine hydrochloride (component 1), glycerol (component 2), and water; DES3: proline (component 1), malic acid (component 2), and water; DES4: choline chloride (component 1), malic acid (component 2), and water.</p>
Full article ">Figure 2
<p>Synthesis (blue), characterization (green), and application (red) of DESs.</p>
Full article ">Figure 3
<p>Four deep eutectic solvents were synthesized according to a constrained mixture design.</p>
Full article ">Figure 4
<p>Contour plots for different DESs densities and viscosities. DES1: guanidine hydrochloride, fructose, and water; DES2: guanidine hydrochloride, glycerol, and water; DES3: proline, malic acid, and water; DES4: choline chloride, malic, acid and water.</p>
Full article ">Figure 4 Cont.
<p>Contour plots for different DESs densities and viscosities. DES1: guanidine hydrochloride, fructose, and water; DES2: guanidine hydrochloride, glycerol, and water; DES3: proline, malic acid, and water; DES4: choline chloride, malic, acid and water.</p>
Full article ">Figure 5
<p>Infrared spectra of the initial reagents and the DESs synthesized using (<b>a</b>) guanidine hydrochloride, fructose, water (DES1); (<b>b</b>) guanidine hydrochloride, glycerol, water (DES2); (<b>c</b>) proline, malic acid, water (DES3); (<b>d</b>) choline chloride, malic acid, water (DES4).</p>
Full article ">Figure 6
<p>NMR hydrogen spectra of the initial reagents and the DESs synthesized using (<b>a</b>) guanidine hydrochloride, fructose, water (DES1); (<b>b</b>) guanidine hydrochloride, glycerol, water (DES2); (<b>c</b>) proline, malic acid, water (DES3); (<b>d</b>) choline chloride, malic acid, water (DES4).</p>
Full article ">Figure 7
<p>(<b>a</b>) Total selenium content in selenium-enriched rice extracted by traditional microwave digestion and different deep eutectic solvents. (<b>b</b>) Recovery values of different pretreatment methods.</p>
Full article ">
16 pages, 274 KiB  
Article
Effects of Household Cooking on Mineral Composition and Retention in Widespread Italian Vegetables
by Silvia Lisciani, Altero Aguzzi, Paolo Gabrielli, Emanuela Camilli, Loretta Gambelli, Luisa Marletta and Stefania Marconi
Nutrients 2025, 17(3), 423; https://doi.org/10.3390/nu17030423 - 24 Jan 2025
Viewed by 401
Abstract
Background/Objectives: The process of cooking food can result in alterations to its nutrient composition due to changes in water content and the destruction or loss of certain micronutrients that occur in response to heat. This study examined the impact of diverse cooking techniques, [...] Read more.
Background/Objectives: The process of cooking food can result in alterations to its nutrient composition due to changes in water content and the destruction or loss of certain micronutrients that occur in response to heat. This study examined the impact of diverse cooking techniques, namely grilling, microwave, and steam, on the macronutrients and minerals of vegetables commonly utilized in Italian cuisine (two varieties of zucchini, eggplants, and potatoes). Methods: The proximate composition was determined according to the Association of Official Analytical Chemists (AOAC) methods. The content of the minerals (Ca, K, P, Mg, Na, Fe, Zn, and Mn) was determined via ICP plasma after liquid washing. Results: Regarding macronutrients, the results revealed a notable difference in the carbohydrate profiles, whereas mineral retention demonstrated considerable heterogeneity. Some minerals, such as Na, Ca, Mn, and Fe, were found to be more prone to significant increases or losses. Moreover, the true retention factor (TR) calculations indicated that microwave cooking resulted in higher retention compared to the other methods for zucchini, while grilling demonstrated higher TR than microwave cooking for eggplants. Potatoes exhibited lower TR values than the other vegetables and their steaming resulted in higher retention than microwave cooking for K, P, Fe, and Zn. Conclusions: The results confirm the heterogeneous behaviors of minerals in commonly consumed Italian vegetables subjected to different cooking methods. The data underscore the need for additional research to understand the effects of heat treatments on mineral profiles and to determine specific retention factors linked to various cooking techniques. The significant gap between “true” and “apparent” retention factors, caused by changes in water content during cooking, highlight the need for new experimental data to update and enrich the existing literature on this topic. Full article
(This article belongs to the Section Nutritional Policies and Education for Health Promotion)
138 pages, 31774 KiB  
Review
Green Ammonia, Nitric Acid, Advanced Fertilizer and Electricity Production with In Situ CO2 Capture and Utilization by Integrated Intensified Nonthermal Plasma Catalytic Processes: A Technology Transfer Review for Distributed Biorefineries
by Galip Akay
Catalysts 2025, 15(2), 105; https://doi.org/10.3390/catal15020105 - 22 Jan 2025
Viewed by 404
Abstract
An Integrated Process Intensification (IPI) technology-based roadmap is proposed for the utilization of renewables (water, air and biomass/unavoidable waste) in the small-scale distributed production of the following primary products: electricity, H2, NH3, HNO3 and symbiotic advanced (SX) fertilizers [...] Read more.
An Integrated Process Intensification (IPI) technology-based roadmap is proposed for the utilization of renewables (water, air and biomass/unavoidable waste) in the small-scale distributed production of the following primary products: electricity, H2, NH3, HNO3 and symbiotic advanced (SX) fertilizers with CO2 mineralization capacity to achieve negative CO2 emission. Such a production platform is an integrated intensified biorefinery (IIBR), used as an alternative to large-scale centralized production which relies on green electricity and CCUS. Hence, the capacity and availability of the renewable biomass and unavoidable waste were examined. The critical elements of the IIBR include gasification/syngas production; syngas cleaning; electricity generation; and the conversion of clean syngas (which contains H2, CO, CH4, CO2 and N2) to the primary products using nonthermal plasma catalytic reactors with in situ NH3 sequestration for SA fertilizers. The status of these critical elements is critically reviewed with regard to their techno-economics and suitability for industrial applications. Using novel gasifiers powered by a combination of CO2, H2O and O2-enhanced air as the oxidant, it is possible to obtain syngas with high H2 concentration suitable for NH3 synthesis. Gasifier performances for syngas generation and cleaning, electricity production and emissions are evaluated and compared with gasifiers at 50 kWe and 1–2 MWe scales. The catalyst and plasma catalytic reactor systems for NH3 production with or without in situ reactive sequestration are considered in detail. The performance of the catalysts in different plasma reactions is widely different. The high intensity power (HIP) processing of perovskite (barium titanate) and unary/binary spinel oxide catalysts (or their combination) performs best in several syntheses, including NH3 production, NOx from air and fertigation fertilizers from plasma-activated water. These catalysts can be represented as BaTi1−vO3−x{#}yNz (black, piezoelectric barium titanate, bp-{BTO}) and M(1)3−jM(2)kO4−m{#}nNr/SiO2 (unary (k = 0) or a binary (k > 0) silane-coated SiO2-supported spinel oxide catalyst, denoted as M/Si = X) where {#} infers oxygen vacancy. HIP processing in air causes oxygen vacancies, nitrogen substitution, the acquisition of piezoelectric state and porosity and chemical/morphological heterogeneity, all of which make the catalysts highly active. Their morphological evaluation indicates the generation of dust particles (leading to porogenesis), 2D-nano/micro plates and structured ribbons, leading to quantum effects under plasma catalytic synthesis, including the acquisition of high-energy particles from the plasma space to prevent product dissociation as a result of electron impact. M/Si = X (X > 1/2) and bp-{BTO} catalysts generate plasma under microwave irradiation (including pulsed microwave) and hence can be used in a packed bed mode in microwave plasma reactors with plasma on and within the pores of the catalyst. Such reactors are suitable for electric-powered small-scale industrial operations. When combined with the in situ reactive separation of NH3 in the so-called Multi-Reaction Zone Reactor using NH3 sequestration agents to create SA fertilizers, the techno-economics of the plasma catalytic synthesis of fertilizers become favorable due to the elimination of product separation costs and the quality of the SA fertilizers which act as an artificial root system. The SA fertilizers provide soil fertility, biodiversity, high yield, efficient water and nutrient use and carbon sequestration through mineralization. They can prevent environmental damage and help plants and crops to adapt to the emerging harsh environmental and climate conditions through the formation of artificial rhizosphere and rhizosheath. The functions of the SA fertilizers should be taken into account when comparing the techno-economics of SA fertilizers with current fertilizers. Full article
(This article belongs to the Special Issue Catalysis for CO2 Conversion, 2nd Edition)
Show Figures

Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>Carbon dioxide emission reduction prediction in IEA “Net Zero by 2050” report. Reproduced from reference [<xref ref-type="bibr" rid="B2-catalysts-15-00105">2</xref>] with permission.</p>
Full article ">Figure 2
<p>Carbon dioxide capture predictions by IEA in 2021 and 2023. Reproduced from reference [<xref ref-type="bibr" rid="B4-catalysts-15-00105">4</xref>] with permission.</p>
Full article ">Figure 3
<p>Energy value (in EJ/year) of various waste and biomass streams as a function of time leading to NZE target of 2050. Reproduced from reference [<xref ref-type="bibr" rid="B2-catalysts-15-00105">2</xref>].</p>
Full article ">Figure 4
<p>Total final energy consumption estimates of IAE by sector and fuel. Reproduced from reference [<xref ref-type="bibr" rid="B2-catalysts-15-00105">2</xref>].</p>
Full article ">Figure 5
<p>Share of feedstock and energy carriers in hydrogen production in the EU28 in the two scenarios (CPI and CAP) for 2030 and 2050. CPI: current policy initiative; CAP: long-term decarbonization. Reproduced from reference [<xref ref-type="bibr" rid="B59-catalysts-15-00105">59</xref>] with permission.</p>
Full article ">Figure 6
<p>Process intensified fixed-bed gasifier systems developed at Newcastle University/UK by the present author over a period of two decades, scaled up from 10 kWe to 1 MWe and then to 2 MWe and its cost comparison with a fluidized bed gasifier. (<bold>a</bold>) 5 MWe fluidized bed gasifier with capital cost of GBP 6m/MWe at 2006 prices. (<bold>b</bold>–<bold>e</bold>) 1 MWe fixed bed-down draft gasifier with specific capital cost of GBP 2m/MWe (2006) [<xref ref-type="bibr" rid="B46-catalysts-15-00105">46</xref>]. (<bold>c</bold>) Orange-colored flare before syngas cleaning; (<bold>d</bold>) blue-colored flame after syngas cleaning using PolyHIPE Polymer; [<xref ref-type="bibr" rid="B46-catalysts-15-00105">46</xref>] (<bold>e</bold>) PolyHIPE Polymer packed bed syngas cleaner; (<bold>f</bold>) Scanning Electron Micrograph (SEM) image of PolyHIPE Polymer before been used in syngas cleaning (Scale bar = 5 μm); (<bold>g</bold>) Advanced and 2 MWe capacity version of the above described gasifier reactor and syngas cleaner; (<bold>h</bold>) one of the internal combustion engines (500 MWe output) used for electricity generator from the 2 MWe-gasifier; (<bold>i</bold>) 50 kWe capacity gasifier operatable with air, O<sub>2</sub>-enhanced air, H<sub>2</sub>O or CO<sub>2</sub> or their binary/ternary combination for enhanced H<sub>2</sub> generation suitable for direct conversion of syngas-to-ammonia fertilizer [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>,<xref ref-type="bibr" rid="B40-catalysts-15-00105">40</xref>].</p>
Full article ">Figure 6 Cont.
<p>Process intensified fixed-bed gasifier systems developed at Newcastle University/UK by the present author over a period of two decades, scaled up from 10 kWe to 1 MWe and then to 2 MWe and its cost comparison with a fluidized bed gasifier. (<bold>a</bold>) 5 MWe fluidized bed gasifier with capital cost of GBP 6m/MWe at 2006 prices. (<bold>b</bold>–<bold>e</bold>) 1 MWe fixed bed-down draft gasifier with specific capital cost of GBP 2m/MWe (2006) [<xref ref-type="bibr" rid="B46-catalysts-15-00105">46</xref>]. (<bold>c</bold>) Orange-colored flare before syngas cleaning; (<bold>d</bold>) blue-colored flame after syngas cleaning using PolyHIPE Polymer; [<xref ref-type="bibr" rid="B46-catalysts-15-00105">46</xref>] (<bold>e</bold>) PolyHIPE Polymer packed bed syngas cleaner; (<bold>f</bold>) Scanning Electron Micrograph (SEM) image of PolyHIPE Polymer before been used in syngas cleaning (Scale bar = 5 μm); (<bold>g</bold>) Advanced and 2 MWe capacity version of the above described gasifier reactor and syngas cleaner; (<bold>h</bold>) one of the internal combustion engines (500 MWe output) used for electricity generator from the 2 MWe-gasifier; (<bold>i</bold>) 50 kWe capacity gasifier operatable with air, O<sub>2</sub>-enhanced air, H<sub>2</sub>O or CO<sub>2</sub> or their binary/ternary combination for enhanced H<sub>2</sub> generation suitable for direct conversion of syngas-to-ammonia fertilizer [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>,<xref ref-type="bibr" rid="B40-catalysts-15-00105">40</xref>].</p>
Full article ">Figure 7
<p>Demonstration of the trophistic function of S fertilizer media (sulfonated-neutralized PolyHIPE Polymer, sn-PHP) by grass cultivated with or without sn-PHP. (<bold>a</bold>) The appearance of root after 3 weeks of growth with or without sn-PHP. (<bold>b</bold>) Enhancement of grass shoot and root due to the presence of two sn-PHP disks as the carrier for water and nutrients. From G. Akay and S. Fleming (in preparation for submission).</p>
Full article ">Figure 8
<p>Nitric oxide (NO) evolution at 25 °C during pulsed microwave irradiation of BaTiO<sub>3−x</sub>{#}<sub>y</sub>N<sub>z</sub> spheres in air with peak power at 200 W for a period of 10 s and no irradiation for 20 s. Nitric oxide concentration [NO] is measured online with maximum detection limit of 500 ppm. The continuous microwave irradiation results in reaching the detection limit in 30 s. Reproduced from reference [<xref ref-type="bibr" rid="B108-catalysts-15-00105">108</xref>] with permission.</p>
Full article ">Figure 9
<p>Schematic diagram of some of the most important species in plasma-activated liquids (water). Reproduced from reference [<xref ref-type="bibr" rid="B113-catalysts-15-00105">113</xref>] with permission.</p>
Full article ">Figure 10
<p>The effect of plasma interactive catalysts on the nitrate, nitrite, ammonium ion and hydrogen peroxide generation in PAW in nitrogen plasma compared with non-catalyst operation (water only). Reproduced from reference [<xref ref-type="bibr" rid="B115-catalysts-15-00105">115</xref>] with permission.</p>
Full article ">Figure 11
<p>Two-stage PNOCRA process scheme with polymer exchange membrane electrolyzer (PEMEL) for the generation of O<sub>2</sub> and H<sub>2</sub>. Stage 1: plasma-assisted N<sub>2</sub>-oxidation, followed by NO<sub>x</sub> adsorption on a Lean NO<sub>x</sub> trap (LNT); Stage 2: catalytic operation of the LNT to reduce the adsorbed NO<sub>x</sub> with H<sub>2</sub> to NH<sub>3</sub> and followed by NH<sub>3</sub> extraction with water. Reproduced from reference [<xref ref-type="bibr" rid="B124-catalysts-15-00105">124</xref>] with permission. Original technique by Hollevoet et al. [<xref ref-type="bibr" rid="B125-catalysts-15-00105">125</xref>,<xref ref-type="bibr" rid="B126-catalysts-15-00105">126</xref>].</p>
Full article ">Figure 12
<p>Schematic illustration of the direct nitrate reduction routes. Reproduced from reference [<xref ref-type="bibr" rid="B132-catalysts-15-00105">132</xref>] with permission.</p>
Full article ">Figure 13
<p>Simplified process flow diagram of hydrogen production from natural gas with carbon capture and storage. Reproduced from reference [<xref ref-type="bibr" rid="B147-catalysts-15-00105">147</xref>] with permission.</p>
Full article ">Figure 14
<p>Comparison of the theoretical energy consumption of various nitrogen fixation processes. Reprinted from reference [<xref ref-type="bibr" rid="B105-catalysts-15-00105">105</xref>] with permission.</p>
Full article ">Figure 15
<p>The current and theoretical energy costs of NH<sub>3</sub> production by electrolysis, nonthermal plasma and looping techniques compared with the HB process. Reproduced from reference [<xref ref-type="bibr" rid="B163-catalysts-15-00105">163</xref>] with permission.</p>
Full article ">Figure 16
<p>Basic DBD plasma reactor with non-porous walls made from quartz. (1) Outer wall, (2) high-voltage central electrode, (3) inlet for the reactants, (4) glass wool, (5) catalyst and PCP space, (6) ground electrode, (7) product outlet. Reproduced from references [<xref ref-type="bibr" rid="B29-catalysts-15-00105">29</xref>,<xref ref-type="bibr" rid="B40-catalysts-15-00105">40</xref>] with permission.</p>
Full article ">Figure 17
<p>Electrode configurations in concentric cylinder DBD reactors. (<bold>a</bold>) Reactor-1: Both electrodes are isolate through the quartz reactor wall and hence are not in contact with the plasma catalysis promoter (PCP) and/or catalyst. (<bold>b</bold>) Reactor-2: High-voltage electrode is isolated and the counter electrode is in contact with the PCPs and/or catalyst. (<bold>c</bold>) Reactor-3: Both electrodes are in contact with the PCP and/or catalyst. Reproduced from references [<xref ref-type="bibr" rid="B29-catalysts-15-00105">29</xref>,<xref ref-type="bibr" rid="B40-catalysts-15-00105">40</xref>] with permission.</p>
Full article ">Figure 18
<p>Diagrammatic illustration of a general purpose DBD plasma catalytic synthesis experimental rig showing: Reactant (feed) gas cylinders, mass-flow controllers (MFCs), Gas mixer, Plasma Reactor-1 (corresponding to Electrode Configuration-1), Product gas analysis through online GC, Data logging and two stage liquid trap (Ice water) and (Dry ice) for off-line liquid product analyses and Reference gas (N<sub>2</sub>) tank supply for the GC. Numbers refer to the full description of the corresponding equipment which is available in reference [<xref ref-type="bibr" rid="B40-catalysts-15-00105">40</xref>]. For example, no=209 refers to the plasma zone. Reproduced from references [<xref ref-type="bibr" rid="B40-catalysts-15-00105">40</xref>] with permission.</p>
Full article ">Figure 19
<p>Multi-Reaction Zone Catalytic Reactor (M-RZR) with application to ammonia synthesis (@RZ-1) and its subsequent sequestration either @RZ-2 (reaction with CO<sub>2</sub> to obtain ammonium carbamate for urea production or anhydrous NH<sub>3</sub> after decomposition and separation) or @RZ-3 (neutralization with acid within the pores of a carrier, such as sulfonated PolyHIPE Polymer, S-PHP). For general applications of the M-RZR system, the reactants A<sub>1</sub> and A<sub>2</sub> enter into the reaction zone RZ-1 and form two gaseous products B<sub>1</sub> and B<sub>2</sub>. They are sequestrated separately by the sequestration agents, A<sub>3</sub> and A<sub>4</sub> at the reaction zones RZ-3 and RZ-2, respectively, thus forming the products, B<sub>3</sub> and B<sub>4</sub>. Reproduced from references [<xref ref-type="bibr" rid="B29-catalysts-15-00105">29</xref>] with permission.</p>
Full article ">Figure 20
<p>Two-reaction zone M-RZR concentric cylinder reactor consisting of catalytic plasma reaction zone (Reaction Zone-1) and product sequestration zone packed with absorbent particles (Reaction Zone-2). The Reaction Zone-1 is similar in design to that shown in <xref ref-type="fig" rid="catalysts-15-00105-f016">Figure 16</xref>, except: (1) the outer quartz wall of the reactor is porous; (2) cooling fluid circulation is present in the plasma zone; (3) Reaction product can preferentially diffuse into the Reaction Zone-2 where they are sequestrated. Unreacted gases are removed from the Reaction Zone-2. Reproduced from reference [<xref ref-type="bibr" rid="B39-catalysts-15-00105">39</xref>] with permission.</p>
Full article ">Figure 21
<p>Variation in energy consumption/cost (E<sub>C</sub>) with ammonia outlet concentration (C<sub>o</sub>) for various plasma processes compared with the Haber–Bosch process. Reproduced from references [<xref ref-type="bibr" rid="B157-catalysts-15-00105">157</xref>] with permission.</p>
Full article ">Figure 22
<p>Technoeconomic evaluation of small-scale plasma catalysis process compared with Haber–Bosch processes at 10 MW (Technology Readiness Level, TRL = 7–9) and 10 kW (TRL = 5–6) scales. TRL for plasma catalytic process at 10 kW is TRL = 1–3. Reproduced from references [<xref ref-type="bibr" rid="B161-catalysts-15-00105">161</xref>] with permission.</p>
Full article ">Figure 23
<p>Schematic diagram of (<bold>A</bold>) a typical conventional methane-fed Haber–Bosch process and (<bold>B</bold>) an electrically powered alternative. Hydrogen and ammonia production stages are separated for illustration purposes to identify similitudes and differences between both technologies. Yellow lines are process gas, dark blue lines are water/steam, light blue lines are air, purple lines are ammonia and dashed lines are electricity. Reproduced from reference [<xref ref-type="bibr" rid="B186-catalysts-15-00105">186</xref>] with permission.</p>
Full article ">Figure 24
<p>Comparison of methane-fed and electrified Haber–Bosch process energy losses. The data for electrically driven process is extrapolated from the methane-fed process using more efficient compressors and typical efficiencies for current alkaline and proton exchange membrane (PEM) electrolyzers, in addition to efficient PEM electrolyzers projected available in the medium term and solid oxide electrolyzers. The data for the efficient electrolysis and HB with in situ absorption includes a hypothetical 90% efficient electrolyzer and a low pressure (3 bar) HB process with in situ ammonia absorption. Reproduced from reference [<xref ref-type="bibr" rid="B186-catalysts-15-00105">186</xref>] with permission.</p>
Full article ">Figure 25
<p>Diagrammatic illustration of coproduction of ammonia and hydrogen using plasma processing. Reproduced from reference [<xref ref-type="bibr" rid="B41-catalysts-15-00105">41</xref>] with permission.</p>
Full article ">Figure 26
<p>Variation in energy efficiency (E<sub>E</sub>), outlet NH<sub>3</sub> concentration (C<sub>o</sub>) and temperature with specific energy input (SEI) in a DPD reactor. (○) Energy efficiency; (<named-content content-type="color:#4022F2">∆</named-content>) Temperature; (<named-content content-type="color:#fc1414">☆</named-content>) Outlet Ammonia concentration. Reproduced from reference [<xref ref-type="bibr" rid="B211-catalysts-15-00105">211</xref>] with permission.</p>
Full article ">Figure 27
<p>Process flow diagram of the integrated process for biomass gasification and ammonia synthesis based on Haber–Bosch process. Reproduced from reference [<xref ref-type="bibr" rid="B214-catalysts-15-00105">214</xref>] with permission.</p>
Full article ">Figure 28
<p>Circular economy of biomass: gasification system for syngas generation/cleaning, syngas-to-NH<sub>3</sub>/fertilizer conversion reactor (M-RZR shown in <xref ref-type="fig" rid="catalysts-15-00105-f019">Figure 19</xref>), use of fertilizers (HB and SX fertilizers), ammonia absorbent for its sequestration (acidic sulfonated PolyHIPE Polymer, s-PHP) and its use as the skeletal structure of the SX fertilizers in agriculture and finally a catalyst for the syngas-to-ammonia synthesis. Reproduced from reference [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>] with permission.</p>
Full article ">Figure 29
<p>Flow diagram of integrated intensified biorefinery (IIPR) for the self-contained biomass-based sustainable circular technology, producing power, energy, H<sub>2</sub>, HNO<sub>3</sub>, NH<sub>3</sub>, urea and symbiotic-smart fertilizers from air (A) and water (W) with CO<sub>2</sub> utilization. Individual unit processes are as follows: (1) Gasifier with in situ oxygen-nitrogen separation, bio-ash (BA) recycle (as combustion catalyst in gasifier) and two-stage syngas cleaning, SC-1 (for power generation) and SC-2 (for syngas conversion to ammonium carbamate (AC), urea and symbiotic-smart fertilizers (S-F). (2) Plasma-generating chemical-looping silica supported catalyst packed plasma reactors PR-1 (plasma nitrogen fixation with NO<sub>x</sub> generation) and PR-2 for catalyst regeneration (with periodic water injection) and hydrogen production. (3) Multi-Reaction Zone Reactor (M-RZR) operating with plasma for direct conversion of syngas to ammonia or ammonia-based fertilizer using soil additives–acid carriers (SA-AC) such as sulfonated PolyHIPE Polymers. (4) NO<sub>x</sub> generated in PR-1 together with unreacted nitrogen are oxidized with oxygen in the Nitric Acid Reactor (NAR) to produce HNO<sub>3</sub> and the unreacted nitrogen and oxygen are returned to the Plasma Reactor-3 (PR-3). Bio-ash (BA) and Bio-tar (BT) from the gasifier are utilized in agriculture as nutrients and herbicides while the agricultural and biowaste provide the feedstock for the gasifier. Bio-ash is also recycled into the gasifier as a source of a cocktail of combustion catalysts. Renewable feedstock is indicated by cyan coloring and the products are highlighted in yellow.</p>
Full article ">Figure 30
<p>Concentrations of ash forming elements in: (<bold>a</bold>) bio-ash, (<bold>b</bold>) syngas after the gasification of sugar cane bagasse [<xref ref-type="bibr" rid="B227-catalysts-15-00105">227</xref>]. Note that in (<bold>b</bold>), the graph is divided into two between K and Mg with different scales. Reproduced from reference [<xref ref-type="bibr" rid="B227-catalysts-15-00105">227</xref>] with permission.</p>
Full article ">Figure 31
<p>Plasma and catalyst interactions. Reproduced from reference [<xref ref-type="bibr" rid="B260-catalysts-15-00105">260</xref>] with permission.</p>
Full article ">Figure 32
<p>XRD pattern of the micro-porous nickel catalyst at various stages of processing (A,B,C) and after being continuously used for 72 h in ammonia synthesis. Nickel catalyst is supported on SiO<sub>2</sub> at a molar ratio of Ni/Si = 1/4. (a) Microwave synthesis from the catalyst and supported precursor fluid (Ni/Si = 1/4 A); (b) Heat treatment of sample from stage-A at 600 C (Ni/Si = 1/4 AB); (c) Reduction in sample from stage-B at 550 °C in hydrogen for 24 h (Ni/Si = 1/4 ABC); (d) After continuous synthesis of ammonia for 72 h (Ni/Si = 1/4 ABCD). XRD-based crystallite sizes at the dominant peaks are summarized in <xref ref-type="table" rid="catalysts-15-00105-t013">Table 13</xref>. Reproduced from reference [<xref ref-type="bibr" rid="B43-catalysts-15-00105">43</xref>] with permission.</p>
Full article ">Figure 33
<p>XRD diffraction patterns of the silica supported binary metal catalysts Cr:Fe:Si (1:1:1) and Cr:Cu:Si (1:1:1) before and after plasma fertigation experiments. Reproduced from reference [<xref ref-type="bibr" rid="B115-catalysts-15-00105">115</xref>] with permission.</p>
Full article ">Figure 34
<p>Structural change of BaTiO<sub>3</sub> after 80 h of direct non-oxidative methane conversion to H<sub>2</sub> and higher hydrocarbons during nonthermal plasma reaction at 100 W power input and 120 °C. (<bold>a</bold>) Surface SEM of fresh stochiometric BaTiO<sub>3</sub> before plasma reaction; (<bold>b</bold>) Surface SEM of the BaTiO<sub>3</sub> after plasma reaction. Details of the experimental conditions are available in References [<xref ref-type="bibr" rid="B173-catalysts-15-00105">173</xref>,<xref ref-type="bibr" rid="B176-catalysts-15-00105">176</xref>]. Reproduced from reference [<xref ref-type="bibr" rid="B176-catalysts-15-00105">176</xref>] with permission.</p>
Full article ">Figure 35
<p>The effect of heterogeneous BaTiO<sub>3</sub> structure with N and O vacancies and N- and H- doping on the ammonia synthesis rates and mechanism using Fe, Ni, Ru and Co metal catalysts at 400 °C and 9 bar. (<bold>a</bold>) Ammonia synthesis rates over Ru, Co, Ni and Fe supported on BaTiO<sub>3−x</sub>N<sub>y</sub> and BaTiO<sub>3−x</sub>H<sub>x</sub>. (<bold>b</bold>) Mechanism with Fe and Ni on BaTiO<sub>3−x</sub>N<sub>y</sub> support; (<bold>c</bold>) Mechanism with Ru and Co on BaTiO<sub>3−x</sub>H<sub>x</sub> support. Reproduced from reference [<xref ref-type="bibr" rid="B289-catalysts-15-00105">289</xref>] with permission.</p>
Full article ">Figure 36
<p>XRD patterns for various barium titanates. (<bold>a</bold>) stochiometric/ferroelectric BaTiO<sub>3</sub> [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]; (<bold>b</bold>) Expanded XRD patterns at 2θ = 44.9° (002); 2θ = 45.4° (200) showing the intensity reversal at these Bragg angles as an indicator of the transformation of the fresh (F) BaTiO<sub>3</sub> from the ferroelectric/paraelectric state to cream-colored (C) black piezoelectric BaTi<sub>1−v</sub>O<sub>3−x</sub>{#}<sub>y</sub>N<sub>z</sub> with some amorphization and to black-colored (B) substantially converted piezoelectric BaTi<sub>1−v</sub>O<sub>3−x</sub>{#}<sub>y</sub>N<sub>z</sub> with substantial amorphization [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]; (<bold>c</bold>) Comparison of the XRD-patterns of synthesized hexagonal piezoelectric h-BaTiO<sub>3−x</sub>, h-BaTiO<sub>3−x</sub>H<sub>x</sub>, h-BaTiO<sub>3−x</sub>N<sub>y</sub> barium titanates [<xref ref-type="bibr" rid="B289-catalysts-15-00105">289</xref>] and the expanded XRD patterns at 2θ = 30°–32° showing the amorphization as well as the emerging new reflection in these materials; (<bold>d</bold>) Expanded XRD patterns at 2θ = 31.5° (101); 2θ = 31.6° (110) showing the amorphization process as the transformation of the fresh (F) BaTiO<sub>3</sub> from the ferroelectric/paraelectric state with color change to cream (C) and black (B) [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]. (<bold>e</bold>) Expanded XRD patterns at 2θ = 55.95° (112) and 2θ = 56.28° (211) showing the amorphization in the cream and black-colored samples [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]. (<bold>c</bold>) is reproduced from reference [<xref ref-type="bibr" rid="B289-catalysts-15-00105">289</xref>] with permission while the other figures are reproduced from reference [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>] with permission.</p>
Full article ">Figure 36 Cont.
<p>XRD patterns for various barium titanates. (<bold>a</bold>) stochiometric/ferroelectric BaTiO<sub>3</sub> [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]; (<bold>b</bold>) Expanded XRD patterns at 2θ = 44.9° (002); 2θ = 45.4° (200) showing the intensity reversal at these Bragg angles as an indicator of the transformation of the fresh (F) BaTiO<sub>3</sub> from the ferroelectric/paraelectric state to cream-colored (C) black piezoelectric BaTi<sub>1−v</sub>O<sub>3−x</sub>{#}<sub>y</sub>N<sub>z</sub> with some amorphization and to black-colored (B) substantially converted piezoelectric BaTi<sub>1−v</sub>O<sub>3−x</sub>{#}<sub>y</sub>N<sub>z</sub> with substantial amorphization [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]; (<bold>c</bold>) Comparison of the XRD-patterns of synthesized hexagonal piezoelectric h-BaTiO<sub>3−x</sub>, h-BaTiO<sub>3−x</sub>H<sub>x</sub>, h-BaTiO<sub>3−x</sub>N<sub>y</sub> barium titanates [<xref ref-type="bibr" rid="B289-catalysts-15-00105">289</xref>] and the expanded XRD patterns at 2θ = 30°–32° showing the amorphization as well as the emerging new reflection in these materials; (<bold>d</bold>) Expanded XRD patterns at 2θ = 31.5° (101); 2θ = 31.6° (110) showing the amorphization process as the transformation of the fresh (F) BaTiO<sub>3</sub> from the ferroelectric/paraelectric state with color change to cream (C) and black (B) [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]. (<bold>e</bold>) Expanded XRD patterns at 2θ = 55.95° (112) and 2θ = 56.28° (211) showing the amorphization in the cream and black-colored samples [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>]. (<bold>c</bold>) is reproduced from reference [<xref ref-type="bibr" rid="B289-catalysts-15-00105">289</xref>] with permission while the other figures are reproduced from reference [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>] with permission.</p>
Full article ">Figure 37
<p>Reaction pathways predicted by plasma and surface chemical kinetics modeling, leading to NH<sub>3</sub> synthesis in a DBD plasma with catalyst during the microdischarges (<bold>a</bold>) and their afterglows (<bold>b</bold>). Eley-Rideal and Langmuir−Hinshelwood and reaction steps are drawn with red and blue arrows, respectively. (<bold>a</bold>) During the micro-discharges, reactive species are created by electron-impact collisions with the feed gas, and they react further to form NH<sub>3</sub>, but at the same time, NH<sub>3</sub> is also destroyed by electron-impact collisions. (<bold>b</bold>) In the subsequent afterglows, the reactive species created during the microdischarges react further to form NH<sub>3</sub> Via several E-R and L-H reactions. Reproduced from van’t Veer et al. [<xref ref-type="bibr" rid="B291-catalysts-15-00105">291</xref>] with permission.</p>
Full article ">Figure 37 Cont.
<p>Reaction pathways predicted by plasma and surface chemical kinetics modeling, leading to NH<sub>3</sub> synthesis in a DBD plasma with catalyst during the microdischarges (<bold>a</bold>) and their afterglows (<bold>b</bold>). Eley-Rideal and Langmuir−Hinshelwood and reaction steps are drawn with red and blue arrows, respectively. (<bold>a</bold>) During the micro-discharges, reactive species are created by electron-impact collisions with the feed gas, and they react further to form NH<sub>3</sub>, but at the same time, NH<sub>3</sub> is also destroyed by electron-impact collisions. (<bold>b</bold>) In the subsequent afterglows, the reactive species created during the microdischarges react further to form NH<sub>3</sub> Via several E-R and L-H reactions. Reproduced from van’t Veer et al. [<xref ref-type="bibr" rid="B291-catalysts-15-00105">291</xref>] with permission.</p>
Full article ">Figure 38
<p>Single domain ferroelectrics (PbTiO<sub>3</sub>) with oxygen and metal vacancies opposite directional transport of photoexcited charges driven by the polarized internal electric field capable of photochemical reduction/oxidation on the opposite polar surfaces. Specific polar surface can be selectively modified with cocatalyst deposition. Alternatively, surfaces can be modified through epitaxial growth of narrow bandgap semiconductors. When two different narrow bandgap ferroelectrics are deposited, the resulting system mimics natural photosynthesis systems. Reproduced with permission from reference [<xref ref-type="bibr" rid="B349-catalysts-15-00105">349</xref>].</p>
Full article ">Figure 39
<p>Selective growth of anatase TiO<sub>2</sub> islands on the (001¯) facet of ferroelectric PbTiO<sub>3</sub> and their morphology and structure. SEM images of (<bold>a</bold>) the pristine ferroelectric PbTiO<sub>3</sub> single crystals and (<bold>b</bold>) PbTiO<sub>3</sub> single crystals with selectively grown anatase TiO<sub>2</sub> islands on their (001¯) facets. (<bold>c</bold>) High-magnification SEM image of one PbTiO<sub>3</sub> crystal with almost square TiO<sub>2</sub> islands. Reproduced from reference [<xref ref-type="bibr" rid="B356-catalysts-15-00105">356</xref>] with permission.</p>
Full article ">Figure 40
<p>The microwave-generated plasma spectra are compared with the corona discharge (gas discharge) tube air plasma spectra. Nitrogen and oxygen lines are visibly identified in both spectra. Reproduced from reference [<xref ref-type="bibr" rid="B393-catalysts-15-00105">393</xref>] with permission.</p>
Full article ">Figure 41
<p>Domain pattern and its comparison with the theoretical torsional stress distribution in a twisted bar of the same size in a thin single crystal BaTiO<sub>3</sub> platelet. The domain pattern vertex junction does not match with the minimum stress minimum in the theoretical stress pattern which may be due to the type of deformation of the platelet. Red circles and the broken line show the mismatching level of vertex junction between the experimental result and theoretical prediction. Reproduced from reference [<xref ref-type="bibr" rid="B392-catalysts-15-00105">392</xref>] with permission.</p>
Full article ">Figure 42
<p>The evolution of various types of structures in prolonged dielectric barrier discharge (DBD) plasma-treated BaTiO<sub>3</sub> particles at different locations evaluated by SEM. (<bold>a</bold>) Overall appearance of the grains showing the presence of plasma erosion (dust generation) and domain pattern evolution on the surface of the grains near the vertex center and their separation (delamination/incomplete exfoliation) (Scale bar = 10 μm); (<bold>b</bold>) Same as in (<bold>a</bold>) at a higher magnification with pore formation and the inner structure of the pore (Scale bar = 10 μm); (<bold>c</bold>) A fractured grain pattern at the vertex center due to the evolution of exudates from the grain bulk (Scale bar = 1 μm); (<bold>d</bold>) View from the top of the disk-like banded/striated domain pattern at the vertex center showing the formation of lattice exudates and the step/terrace structure on the lateral walls of the disks (Scale bar = 1 μm); (<bold>e</bold>) View from the lateral side of the banded/striated disk-like domain patterns in the form of laminated bundles showing the presence of lattice exudates on them and step-terrace domains as they bifurcate and delaminate (Scale bar = 100 nm); (<bold>f</bold>) Same as in (<bold>e</bold>) at higher magnification showing the range of thickness of the surface domain patterns (Scale bar = 100 nm); (<bold>g</bold>) Illustration of the banded/striated domains on the surface of a grain undergoing bifurcative delamination and reaching to the side of a grain (Scale bar = 1 μm); (<bold>h</bold>) The cross-sectional view of the disk-like domain patters going into the bulk illustrating the generation of the 2D-plates (Scale bar = 1 μm).</p>
Full article ">Figure 42 Cont.
<p>The evolution of various types of structures in prolonged dielectric barrier discharge (DBD) plasma-treated BaTiO<sub>3</sub> particles at different locations evaluated by SEM. (<bold>a</bold>) Overall appearance of the grains showing the presence of plasma erosion (dust generation) and domain pattern evolution on the surface of the grains near the vertex center and their separation (delamination/incomplete exfoliation) (Scale bar = 10 μm); (<bold>b</bold>) Same as in (<bold>a</bold>) at a higher magnification with pore formation and the inner structure of the pore (Scale bar = 10 μm); (<bold>c</bold>) A fractured grain pattern at the vertex center due to the evolution of exudates from the grain bulk (Scale bar = 1 μm); (<bold>d</bold>) View from the top of the disk-like banded/striated domain pattern at the vertex center showing the formation of lattice exudates and the step/terrace structure on the lateral walls of the disks (Scale bar = 1 μm); (<bold>e</bold>) View from the lateral side of the banded/striated disk-like domain patterns in the form of laminated bundles showing the presence of lattice exudates on them and step-terrace domains as they bifurcate and delaminate (Scale bar = 100 nm); (<bold>f</bold>) Same as in (<bold>e</bold>) at higher magnification showing the range of thickness of the surface domain patterns (Scale bar = 100 nm); (<bold>g</bold>) Illustration of the banded/striated domains on the surface of a grain undergoing bifurcative delamination and reaching to the side of a grain (Scale bar = 1 μm); (<bold>h</bold>) The cross-sectional view of the disk-like domain patters going into the bulk illustrating the generation of the 2D-plates (Scale bar = 1 μm).</p>
Full article ">Figure 43
<p>Structure development during the simultaneous microwave and plasma treated HNO<sub>3</sub> doped s-BTO at 1800 W for 10 min. (<bold>a</bold>) A collection of BTO particles illustrating the range of chemical and structural changes due to simultaneous microwave and plasma treatments: samples (1), (2) and (3) represent particle fusion and provide surface charges, sample (4) represents electrical treeing and subsequent fracture and provides changes in the bulk (Scale bar = 1 mm); (<bold>b</bold>) typical surface appearance of sample-(2) at low magnification showing a dusty surface and the structure of the grains below the dust particles (Scale bar = 100 μm); (<bold>c</bold>) domain pattern structure in a pore showing 3 vertex centers and the step-terrace generation around their sides, (Scale bar = 4 μm); (<bold>d</bold>) Appearance of the surface boundary between the fused samples (1) and (3) illustrating the presence of grains (sample-(1) and fused grains on the sample-(3) (Scale bar = 10 μm); (<bold>e</bold>) Surface structure on sample-(1) at high magnification showing several structural features (Scale bar = 1 μm); (<bold>f</bold>) Appearance of domain patterns on the surface of the grains on sample-(2) similar to those described in <xref ref-type="fig" rid="catalysts-15-00105-f042">Figure 42</xref> (Scale bar = 10 μm); (<bold>g</bold>) Enlarged view of (<bold>f</bold>) showing the generation of the step-terrace structures around the exposed sides of the domain patterns together with single/small and aggregated lattice exudates (Scale bar = 1 μm); (<bold>h</bold>) Further enlargement of the single and aggregated lattice exudates and the step-terrace structures illustrating their fine structure (Scale bar = 100 nm).</p>
Full article ">Figure 43 Cont.
<p>Structure development during the simultaneous microwave and plasma treated HNO<sub>3</sub> doped s-BTO at 1800 W for 10 min. (<bold>a</bold>) A collection of BTO particles illustrating the range of chemical and structural changes due to simultaneous microwave and plasma treatments: samples (1), (2) and (3) represent particle fusion and provide surface charges, sample (4) represents electrical treeing and subsequent fracture and provides changes in the bulk (Scale bar = 1 mm); (<bold>b</bold>) typical surface appearance of sample-(2) at low magnification showing a dusty surface and the structure of the grains below the dust particles (Scale bar = 100 μm); (<bold>c</bold>) domain pattern structure in a pore showing 3 vertex centers and the step-terrace generation around their sides, (Scale bar = 4 μm); (<bold>d</bold>) Appearance of the surface boundary between the fused samples (1) and (3) illustrating the presence of grains (sample-(1) and fused grains on the sample-(3) (Scale bar = 10 μm); (<bold>e</bold>) Surface structure on sample-(1) at high magnification showing several structural features (Scale bar = 1 μm); (<bold>f</bold>) Appearance of domain patterns on the surface of the grains on sample-(2) similar to those described in <xref ref-type="fig" rid="catalysts-15-00105-f042">Figure 42</xref> (Scale bar = 10 μm); (<bold>g</bold>) Enlarged view of (<bold>f</bold>) showing the generation of the step-terrace structures around the exposed sides of the domain patterns together with single/small and aggregated lattice exudates (Scale bar = 1 μm); (<bold>h</bold>) Further enlargement of the single and aggregated lattice exudates and the step-terrace structures illustrating their fine structure (Scale bar = 100 nm).</p>
Full article ">Figure 44
<p>Fracture surface images from sample-(4) illustrating the electrical activity within the bulk of the microwaved BTO. (<bold>a</bold>) Domain pattern formation on the surface of the grains at a location 1 mm from the surface (Scale bar = 10 μm); (<bold>b</bold>) Domain pattern structure on the surface of a grain 1000 μm from the surface of the fracture surface of BTO particle (Scale bar = 1 μm); (<bold>c</bold>) Enlarged view of the domain pattern taken from the side showing the nano-particulate nature of the step-terrace structures (Scale bar = 1 μm); (<bold>d</bold>) Electrical treeing in the bulk of the sample-(4), (Scale bar = 100 μm); (<bold>e</bold>) Enlarged view of the electrical tree showing the presence of the several vertex centers ordered in the formation of the electrical tree (Scale bar = 10 μm); (<bold>f</bold>) Enlarged view of the surface structure of the electrical tree illustrating the presence of surface steps-terraces as well as elongated lattice exudates, (Scale bar = 10 μm); (<bold>g</bold>) Enlarged view of the surface structure of the electrical tree illustrating the lattice exudates in the form of rods (Scale bar = 1 μm); (<bold>h</bold>) Enlarged view of the banded domain patterns in the form of 2D-nanoplates (Scale bar = 100 nm); (<bold>i</bold>) Microstructure of the microwave irradiated BTO near electric tree (Scale bar = 500 μm); (<bold>j</bold>) Porous structure near several electrical trees emanating from the surface, (Scale bar = 500 μm).</p>
Full article ">Figure 44 Cont.
<p>Fracture surface images from sample-(4) illustrating the electrical activity within the bulk of the microwaved BTO. (<bold>a</bold>) Domain pattern formation on the surface of the grains at a location 1 mm from the surface (Scale bar = 10 μm); (<bold>b</bold>) Domain pattern structure on the surface of a grain 1000 μm from the surface of the fracture surface of BTO particle (Scale bar = 1 μm); (<bold>c</bold>) Enlarged view of the domain pattern taken from the side showing the nano-particulate nature of the step-terrace structures (Scale bar = 1 μm); (<bold>d</bold>) Electrical treeing in the bulk of the sample-(4), (Scale bar = 100 μm); (<bold>e</bold>) Enlarged view of the electrical tree showing the presence of the several vertex centers ordered in the formation of the electrical tree (Scale bar = 10 μm); (<bold>f</bold>) Enlarged view of the surface structure of the electrical tree illustrating the presence of surface steps-terraces as well as elongated lattice exudates, (Scale bar = 10 μm); (<bold>g</bold>) Enlarged view of the surface structure of the electrical tree illustrating the lattice exudates in the form of rods (Scale bar = 1 μm); (<bold>h</bold>) Enlarged view of the banded domain patterns in the form of 2D-nanoplates (Scale bar = 100 nm); (<bold>i</bold>) Microstructure of the microwave irradiated BTO near electric tree (Scale bar = 500 μm); (<bold>j</bold>) Porous structure near several electrical trees emanating from the surface, (Scale bar = 500 μm).</p>
Full article ">Figure 45
<p>Location of the energy-dispersive X-ray spectra for the elemental analysis at various locations after the microwave irradiation of HNO<sub>3</sub> doped s-BTO in air. (<bold>a</bold>) There are two locations for the EDX-spectra; Spectrum-1 is taken over the region of fused domains generated by electrical trees shown in <xref ref-type="fig" rid="catalysts-15-00105-f044">Figure 44</xref>i; and Spectrum-2 is taken over a dusty zone of the same region; (Scale bar = 250 μm); (<bold>b</bold>) Surface of the BTO sphere showing the presence of partially fused large grains covered with dust particles, (Scale bar = 250 μm); (<bold>c</bold>) Electrical tree and the surrounding area of fused domains, (Scale bar = 250 μm); (<bold>d</bold>) Surface of the electrical tree at high magnification showing a number of platelets formed by the aggregated lattice exudates, (Scale bar = 25 μm).</p>
Full article ">Figure 45 Cont.
<p>Location of the energy-dispersive X-ray spectra for the elemental analysis at various locations after the microwave irradiation of HNO<sub>3</sub> doped s-BTO in air. (<bold>a</bold>) There are two locations for the EDX-spectra; Spectrum-1 is taken over the region of fused domains generated by electrical trees shown in <xref ref-type="fig" rid="catalysts-15-00105-f044">Figure 44</xref>i; and Spectrum-2 is taken over a dusty zone of the same region; (Scale bar = 250 μm); (<bold>b</bold>) Surface of the BTO sphere showing the presence of partially fused large grains covered with dust particles, (Scale bar = 250 μm); (<bold>c</bold>) Electrical tree and the surrounding area of fused domains, (Scale bar = 250 μm); (<bold>d</bold>) Surface of the electrical tree at high magnification showing a number of platelets formed by the aggregated lattice exudates, (Scale bar = 25 μm).</p>
Full article ">Figure 46
<p>The catalyst surface morphology and composition at three specific sites with low, average and high Catalyst/Support ratio. SEM images and the corresponding EDX-spectra of the Co/Si = 2 catalyst at various sites on the surface of the same sample. (<bold>a</bold>,<bold>d</bold>) Lowest cobalt site with [Co] = 0.248; [Si] = 0.085; [O] = 0.667; (<bold>b</bold>,<bold>e</bold>) Average cobalt site with [Co] = 0.659; [Si] = 0.043; [O] = 0.298; (<bold>c</bold>,<bold>f</bold>) Highest cobalt site with [Co] = 0.933; [Si] = 0.007; [O] = 0.060. Scale bar = 1 μm in all SEMs. Note that SiO<sub>2</sub> support is also present within the wall of the catalyst. Reproduced from reference [<xref ref-type="bibr" rid="B108-catalysts-15-00105">108</xref>] with permission.</p>
Full article ">Figure 47
<p>Summary of the characteristics of Co/Si = X catalyst surface as a function of theoretical (feed) catalyst concentration, [Co]<sub>T</sub> = X/(1 + X). (<bold>a</bold>) Variation in concentration of oxygen, [O]<sub>n</sub> (n = 0, 1, 2) with the feed catalyst concentration [Co]<sub>T</sub> at various locations represented by n = 0, 1, 2 (n = 0, average molar concentration; n = 1 where cobalt concentration is the lowest and n = 2 where cobalt concentration is the highest); (<bold>b</bold>) Variation in Log (Cobalt/Silica ratio), Log A<sub>n</sub>, (A<sub>n</sub> = [Co]<sub>n</sub>/[Si]<sub>n</sub>) with theoretical cobalt concentration, [Co]<sub>T</sub> at 3 locations represented by n = 0, 1, 2. Reproduced from reference [<xref ref-type="bibr" rid="B119-catalysts-15-00105">119</xref>] with permission.</p>
Full article ">Figure 48
<p>Decorative structure formation in Co-based binary catalyst. (<bold>a</bold>) Co/Cu/Si = 1/1/8(A), 1 kW, (Scale bar = 2 μm); (<bold>b</bold>) Co/Ni/Si = 1/1/8(A), 1 kW, (Scale bar = 5 μm); (<bold>c</bold>) Co/Cu/Si = 1/1/8(A), 1.8 kW (Scale bar = 1 μm); (<bold>d</bold>) Co/Cu/Si = 1/1/8(A), 1.8 kW, same as (<bold>c</bold>) at high magnification showing the particulate nature of the decorations, (Scale bar = 100 nm).</p>
Full article ">Figure 49
<p>Structure formation in Mn/Cu/Si = 1/0.5/1(A) plasma-generating catalyst produced at 1.8 kW with structure similar to bp-{BTO}. (<bold>a</bold>) Surface structure showing the presence of layering, (Scale bar = 1 μm); (<bold>b</bold>) Fracture surface of the catalyst; (Scale bar = 10 μm); (<bold>c</bold>) Enlarged view of the fracture surface obtained by EDS to illustrate the chemical structure of the catalyst, (Scale bar = 2.5 μm); (<bold>d</bold>) Presence of 2D-planes with step and terrace sites, (Scale bar = 100 nm); (<bold>e</bold>) Mn mapping; (<bold>f</bold>) Cu mapping; (<bold>g</bold>) Si mapping; (<bold>h</bold>) O mapping. Adopted from references [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>,<xref ref-type="bibr" rid="B108-catalysts-15-00105">108</xref>] with permission.</p>
Full article ">Figure 50
<p>Processing and morphological characteristics of the HIP-catalysts using silane coated silica and the formation of “bar-code” nano-ribbons evaluated by transmission electron microscopy. (<bold>a</bold>) Diagrammatic representation of silane coated aggregated silica particle (from Reference [<xref ref-type="bibr" rid="B429-catalysts-15-00105">429</xref>]); (<bold>b</bold>) Image of the catalyst/support precursor fluid (Fe/Si = 1/3) after 30 h photo-irradiation; (<bold>c</bold>) TEM image of Ni/Si = 1/4(A) catalyst showing the planar and particulate nature of the catalyst structure at lower direct magnification (64 k); (<bold>d</bold>–<bold>i</bold>) High direct magnification (450 k) images of the fine structures of various single or binary catalysts showing the “bar-code” structure formation due to silane coating of silica support: (<bold>d</bold>) Ni/Si = 1/4(A); (<bold>e</bold>) Ni/Si = 1/4(ABCD), used in plasma ammonia synthesis; (<bold>f</bold>) Co/Si = 1/4(ABC); (<bold>g</bold>) Fe/Si = 1/4(A) obtained from FeCl<sub>3</sub> (instead of Fe(NO)<sub>3</sub> in all other cases); (<bold>h</bold>) Fe/Mn/Si = 1/1/8(ABC) binary catalyst; (<bold>i</bold>) Fe/Mn/Si = 1/1/8 (Photo-irradiated catalyst. Unlike all the other cases in which microwave radiation was used, this sample was synthesized through photo-irradiation of the catalyst and support precursor solution). (<bold>a</bold>) is reproduced from P. Greenwoon [<xref ref-type="bibr" rid="B429-catalysts-15-00105">429</xref>] with permission.</p>
Full article ">Figure 51
<p>SEM images of bp-{BTO}@{Co/Si = X(J)} core–shell catalyst with Co/Si = 2/1 shell catalyst and bp-{BTO} black piezoelectric core catalyst. (<bold>a</bold>) Overall appearance and surface structure (Scale bar = 100 μm); (<bold>b</bold>) Surface at a higher magnification showing the detail of the Co<sub>3</sub>O<sub>4</sub> morphology (Scale bar = 1 μm); (<bold>c</bold>) Appearance of bp-{BaTiO<sub>3</sub>} below the Co<sub>3</sub>O<sub>4</sub> surface coating showing the porogenesis of ca. 2 μm particles ejected from a large bp-{BTO} particle (Scale bar = 1 μm); (<bold>d</bold>) Detail of the bp-{BTO} particle surface at higher magnification showing the generation of 2D-plates as a result of delamination and phase change in the BTO (Scale bar = 1 μm). Reproduced from reference [<xref ref-type="bibr" rid="B10-catalysts-15-00105">10</xref>] with permission.</p>
Full article ">Figure 52
<p>Generation of a micro-ecology within the symbiotic rhizosphere/rhizosheath (SRS medium) following its use in soil for the cultivation of a legume (pea) plant. (<bold>a</bold>) Fresh SRS medium (Scale bar = 2 μm); (<bold>b</bold>) Root penetration and occupancy of the pores, (Scale bar = 500 μm); (<bold>c</bold>) Generation of a complex microbial environment within the pores of the SRS medium (Scale bar = 2 μm). Reproduced from reference [<xref ref-type="bibr" rid="B33-catalysts-15-00105">33</xref>] with permission.</p>
Full article ">
22 pages, 4764 KiB  
Article
The Effect of Liquids Activated by Plasma Generated with a Microwave Plasmatron and High-Frequency Glow Discharge on Cotton Plant Development
by Sergey A. Shumeyko, Denis V. Yanykin, Mark O. Paskhin, Vladimir I. Lukanin, Dmitry A. Zakharov, Maxim E. Astashev, Roman Y. Pishchalnikov, Ruslan M. Sarimov, Mukhsindjan Kh. Ashurov, Erkindjan M. Ashurov, Dilbar K. Rashidova, Muzaffar M. Yakubov, Aleksei M. Davydov, Victoriya V. Gudkova, Yuri K. Danileyko, Alexey S. Dorokhov and Sergey V. Gudkov
Plants 2025, 14(3), 304; https://doi.org/10.3390/plants14030304 - 21 Jan 2025
Viewed by 454
Abstract
In this study, we investigated the effect of plasma-activated liquids (PAL) on the cotton plant (Gossypium hirsutum L.) growth under laboratory and field conditions. We used two types of PAL: deionized water activated with plasma generated using a microwave plasmatron in atmospheric-pressure [...] Read more.
In this study, we investigated the effect of plasma-activated liquids (PAL) on the cotton plant (Gossypium hirsutum L.) growth under laboratory and field conditions. We used two types of PAL: deionized water activated with plasma generated using a microwave plasmatron in atmospheric-pressure air flow (PAW) and a 1.5% KNO3 solution activated using plasma generated in an electrochemical cell (PAKNO3). These treatments differ in terms of their content of long-lived biologically active compounds. PAW contains a higher concentration of hydrogen peroxide (150 μM compared to 1.1 μM), while PAKNO3 is more saturated with NO2 and NO3 (1510 μM compared to 300 µM). We found that PAW improved cotton plant growth under field conditions and in a laboratory drought stress. Additionally, PAW increased field emergence and germination of heat-treated cotton seeds in the laboratory. It was revealed that PAW prevents the drought-induced disruption of the partitioning of absorbed light energy in the photosynthetic apparatus. Meanwhile, PAKNO3 has a positive effect on seed germination. The positive effect of PALs on cotton seeds and plants is thought to be due to the generation of long-lived biologically active oxygen and nitrogen species during plasma treatment of the liquid. Full article
(This article belongs to the Section Plant Response to Abiotic Stress and Climate Change)
Show Figures

Figure 1

Figure 1
<p>Values maps of fluctuations bispectrality coefficients in the background fluorescence level of not treated (<b>A</b>) and treated plants with plasma-activated water (<b>B</b>).</p>
Full article ">Figure 2
<p>Effect of cotton seeds treatment with pure water (1—black curve) or solution containing 1% PAW (2—red curve), 0.75% PAW (3—green curve) or 0.5% PAW (4—blue curve) for 10 min at room temperature on cotton plant growth in the field. Stars indicate statistically significant difference between the experimental (2, 3 or 4) and control groups (1) of seed (<span class="html-italic">p</span> ≤ 0.05). The data are the means of 40 measurements, with the standard deviation of the mean. Experiment were repeated 4 times.</p>
Full article ">Figure 3
<p>Formation of sympodial branches (<b>A</b>), buds (<b>B</b>), flowers (<b>C</b>), and bolls (<b>D</b>) during the growth of cotton plants in the field. Before planting, cotton seeds were incubated in pure water (1—black curve) or solution containing 0.5% PAW (2—red curve), 0.75% PAW (3—green curve), or 1% PAW (4—blue curve) for 10 min at room temperature. The numbers in parentheses in (<b>D</b>) indicate the proportion of bolls that opened at the end of the growing season. Letters indicate statistically significant difference between different groups (<span class="html-italic">p</span> ≤ 0.05). The data are the means of 40 measurements with the standard deviation of the mean.</p>
Full article ">Figure 4
<p>Effect of water deficit on FW/A (<b>A</b>), DW/A (<b>B</b>) and chlorophyll content (<b>C</b>) in cotton leaves of the cotton in the laboratory. The chlorophyll content in cotton leaves not exposed to drought was taken as 100%, which was 9 r. u. (measured by CL-01), which corresponds to 4.05 mg Chl/g FW (for other details, see <a href="#sec4-plants-14-00304" class="html-sec">Section 4</a>). Plants were grown under normal (unshaded columns) and water deficit (shaded columns) conditions and were watered with a nutrient solution without (control plants and KNO<sub>3</sub> plants) or with a PAL. The designations of plant group below the columns correspond to the designations of the corresponding plant groups in the text. Letters a and b above the columns indicate statistically significant differences between the groups of plants grown under normal conditions (<span class="html-italic">p</span> ≤ 0.05). Letters a’, b’ and c’ indicate statistically significant differences between the groups of plants grown under drought conditions (<span class="html-italic">p</span> ≤ 0.05). * indicate statistically significant effect of water deficit on plants (<span class="html-italic">p</span> ≤ 0.05). The data are the means of 30 measurements with the standard deviation of the mean for FW and DW, and 150 measurements with the standard deviation of the mean for chlorophyll content.</p>
Full article ">Figure 5
<p>Effect of water deficit on the transpiration intensity (<b>A</b>) and the CO<sub>2</sub> assimilation intensity (<b>B</b>) in the leaves of cotton plants grown in laboratory conditions (for more details, see <a href="#sec4-plants-14-00304" class="html-sec">Section 4</a>) watered with a nutrient solution containing no (control plants and KNO<sub>3</sub> plants) and containing PAL. The designations of the plant groups under the columns correspond to the designations of the corresponding plant groups in the text. The plants were pre-adapted to light for 4 h. The measurements were carried out at 27 °C, 40% humidity and CO<sub>2</sub> concentration of 400 ppm and acting light λ = 625 nm, 600 µmol photons m<sup>−2</sup> s<sup>−1</sup>. The rates of CO<sub>2</sub> assimilation and transpiration for plants of each group grown under normal conditions are taken as 100%. * indicate statistically significant difference between effect of water deficit in PAL plants and the corresponding control plants (<span class="html-italic">p</span> ≤ 0.05). The data are the means of eight measurements, with the standard deviation of the mean.</p>
Full article ">Figure 6
<p>Dependence of the parameters ChlF Y(II) (<b>A</b>,<b>D</b>,<b>G</b>), q<sub>N</sub> (<b>B</b>,<b>E</b>,<b>H</b>) and Y(NO) (<b>C</b>,<b>F</b>,<b>I</b>) in cotton plants (control plants (<b>A</b>,<b>B</b>,<b>C</b>), PAW<sub>0.75%</sub> plants (<b>D</b>,<b>E</b>,<b>F</b>) and PAKNO<sub>3</sub> plants (<b>G</b>,<b>H</b>,<b>I</b>)), grown under normal conditions (curve 1) and under water deficit conditions (curve 2) on the intensity of the acting light during light adaptation of cotton plants grown in laboratory. Measurements were carried out at 27 °C, 40% humidity and CO<sub>2</sub> concentration of 400 ppm. Plant adaptation to each intensity of acting light (λ = 625 nm) was 10 min. The data are the mean of three measurements with standard deviations which are smaller than the size of the symbols.</p>
Full article ">Figure 7
<p>Block diagrams of installations for obtaining plasma-activated solutions. Activation was carried out using plasma generated in an electrochemical cell (<b>A</b>), generated by a microwave plasmatron (<b>B</b>). 1—generator, 2—cathode, 3—anode, 4—power source, 5—magnetron, 6—external electrode, 7—internal electrode, 8—quartz capillary, 9—plasma discharge, 10—glass beaker, 11—activated liquid (deionized water in (<b>A</b>) or electrolyte solution in (<b>B</b>)), 12—magnetic mixer, 13—magnetic stirrer.</p>
Full article ">
16 pages, 2256 KiB  
Article
Ultrasound-Assisted Extraction Followed by Inductively Coupled Plasma Mass Spectrometry and Multivariate Profiling of Rare Earth Elements in Coffee
by Aleksandra Savić, Jelena Mutić, Milica Lučić, Jelena Vesković, Andrijana Miletić and Antonije Onjia
Foods 2025, 14(2), 275; https://doi.org/10.3390/foods14020275 - 16 Jan 2025
Viewed by 862
Abstract
A rapid and efficient ultrasound-assisted extraction (UAE) procedure followed by inductively coupled plasma mass spectrometry (ICP-MS) was developed for the determination of 14 rare earth elements (REEs) (La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu), along with [...] Read more.
A rapid and efficient ultrasound-assisted extraction (UAE) procedure followed by inductively coupled plasma mass spectrometry (ICP-MS) was developed for the determination of 14 rare earth elements (REEs) (La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu), along with yttrium (Y) and scandium (Sc), in coffee samples. The method was validated using certified reference material (NIST SRM 1547), recovery tests at four fortification levels, and comparisons with microwave-assisted digestion (MAD). Excellent accuracy and precision were achieved, with recovery rates ranging from 80.1% to 112% and relative standard deviations (RSD%) below 14%. Limits of detection (LODs) ranged from 0.2 ng/kg (Yb) to 0.16 µg/kg (Nd). Total REE concentrations varied between 8.3 µg/kg and 1.1 mg/kg, with the highest individual mean concentrations (µg/kg) observed for Ce (11.7), La (6.0), and Sc (4.7). The lowest individual mean concentrations (µg/kg) were for Ho (0.16), Lu (0.066), and Tm (0.063). Multivariate analysis of REE profiles from 92 coffee samples collected in Serbia revealed clear distinctions between ground roasted and instant coffees, as well as between different surrogate blends. This study indicated that the determination of coffee’s geographical origin was not possible due to the diverse types, blends, and additives. However, differences in REE profiles suggest potential classification based on variety. REEs pose a negligible health risk to coffee consumers, with HI values ranging from 4.7 × 10−8 to 6.3 × 10−6 and TCR ranging from 2.6 × 10−14 to 3.5 × 10−12. Full article
Show Figures

Figure 1

Figure 1
<p>Linear regressions between REE concentrations in coffee after MAD and UAE (<span class="html-italic">n</span> = 10).</p>
Full article ">Figure 2
<p>Box plots of REE concentrations in analyzed coffee samples.</p>
Full article ">Figure 3
<p>Pearson correlation network among concentrations of 16 different REEs in coffee samples (<span class="html-italic">n</span> = 92). Only positive correlations are represented: blue lines indicate strong positive correlations, light blue lines indicate moderate correlations, and the red line indicates weak positive correlations.</p>
Full article ">Figure 4
<p>Principal component analysis (PCA). Score plot for 92 coffee samples based on rare earth element (REE) concentrations: blue ►—ground roasted coffees; orange ◄—instant coffees; violet ▲—instant coffees with additives; pink ♦—ground roasted coffees in capsules; red ●—surrogates for coffee; red star—coffees with surrogates (2% chickpeas).</p>
Full article ">Figure 5
<p>Heatmap dendrogram for the coffee samples and rare earth elements (REEs).</p>
Full article ">Figure 6
<p>PMF results illustrate the contribution of REEs to three different factors.</p>
Full article ">Figure 7
<p>Contribution of REEs to the hazard index (HI) and target cancer risk (TCR) from coffee.</p>
Full article ">
14 pages, 4308 KiB  
Article
Microwave Plasma-Driven Synthesis of Graphene and N-Graphene at a Gram Scale
by Neli Bundaleska, Edgar Felizardo, Ana Dias, Ana Maria Ferraria, Ana Maria Botelho do Rego, Janez Zavašnik, Uros Cvelbar, Miroslav Abrashev, Jivko Kissovski, Amélia Almeida, Luís Lemos Alves, Bruno Gonçalves and Elena Tatarova
Processes 2025, 13(1), 196; https://doi.org/10.3390/pr13010196 - 12 Jan 2025
Viewed by 531
Abstract
The large-scale microwave plasma synthesis of graphene and nitrogen-doped graphene with tailored structural properties, crucial for their successful usage applications, has been demonstrated. The developed atmospheric pressure plasma method offers several advantages, including the continuous production of high-quality, free-standing graphene without the use [...] Read more.
The large-scale microwave plasma synthesis of graphene and nitrogen-doped graphene with tailored structural properties, crucial for their successful usage applications, has been demonstrated. The developed atmospheric pressure plasma method offers several advantages, including the continuous production of high-quality, free-standing graphene without the use of chemicals, solvents, catalysts, or additional heating. This non-toxic process eliminates the need for vacuum systems while achieving high temperatures. The method enables the precise control over graphene’s properties, such as the layer number, defects, sheet size, uniformity, and functionality, as well as the doping type and configuration, by adjusting the plasma parameters. Protocols for the synthesis of specific nanostructures with a controlled structural quality, production rate, and chemical composition have been established using methane and methylamine as precursors. The comprehensive physicochemical characterization of the graphene and nitrogen-doped graphene was carried out using scanning electron microscopy, high-resolution transmission electron microscopy, Raman spectroscopy, X-ray diffraction, and X-ray photoelectron spectroscopy. Full article
(This article belongs to the Special Issue Atmospheric Pressure Plasma Technologies and Applications)
Show Figures

Figure 1

Figure 1
<p>Schematic representation of the plasma prototype.</p>
Full article ">Figure 2
<p>Infrared absorption spectra of the (<b>a</b>) Ar/methane and (<b>b</b>) Ar/methane/methylamine outlet gas with the plasma on and off.</p>
Full article ">Figure 3
<p>Raman spectra of (<b>a</b>) #MG1 (Q<sub>CH4</sub> = 100 sccm) and (<b>b</b>) #MG3 (Q<sub>CH4</sub> = 150 sccm) at randomly chosen locations, (<b>c</b>) the SEM, (<b>d</b>) the XRD pattern of the graphene fabricated with methane (Q<sub>CH4</sub> = 150 sccm), (<b>e</b>) the XPS survey spectrum, and (<b>f</b>) the C 1s region of the graphene synthesized with methane (Q<sub>CH4</sub> = 150 sccm). Synthesis conditions: #MG1 and #MG3.</p>
Full article ">Figure 4
<p>(<b>a</b>,<b>b</b>) Raman spectra, (<b>c</b>) XRD patterns, (<b>d</b>,<b>e</b>) TEM micrographs of #T8 and #T22, (<b>f</b>) XPS survey spectra, (<b>g</b>,<b>h</b>) XPS C 1s regions, (<b>i</b>) XPS quantification/atomic concentrations (%), and relevant atomic ratios. Synthesis conditions: #T8 and #T22.</p>
Full article ">Figure 5
<p>(<b>a</b>) Raman spectra collected from different locations, (<b>b</b>) the XRD pattern, (<b>c</b>,<b>d</b>) the TEM micrographs, (<b>e</b>–<b>g</b>) the XPS survey, and the C 1s, and N 1s regions, respectively, detected from the N-graphene synthesized with methane/methylamine in the top-down injection.</p>
Full article ">Figure 6
<p>(<b>a</b>) Raman spectra collected from different locations, (<b>b</b>) the XRD pattern, (<b>c</b>) the particle size distribution, (<b>d</b>) the SEM and (<b>e</b>) TEM micrographs, and (<b>f</b>–<b>h</b>) the survey of the XPS spectrum, the C 1s region, and the N 1s region, respectively, from the N-graphene synthesized with methane/methylamine in the top-down injection + bottom-up methylamine.</p>
Full article ">
25 pages, 9131 KiB  
Review
Completion of Waste Heat Recovery and CO2 Conversion Simultaneously Based on the Flue Gas Chemical Recuperative Cycle: A Review
by Mengze He, Ping Zhou, Xiqiang Zhao and Tao Wang
Energies 2025, 18(2), 232; https://doi.org/10.3390/en18020232 - 7 Jan 2025
Viewed by 520
Abstract
Energy shortage and greenhouse gas emission have become bottlenecks in current society development. Improving the efficiency of energy conversion and utilization systems through waste heat recovery and reduction of greenhouse gas through CO2 capture/conversion are important solutions. Both can be achieved simultaneously [...] Read more.
Energy shortage and greenhouse gas emission have become bottlenecks in current society development. Improving the efficiency of energy conversion and utilization systems through waste heat recovery and reduction of greenhouse gas through CO2 capture/conversion are important solutions. Both can be achieved simultaneously by utilizing high-temperature flue gas or CO2 in flue gas for organic matter gasification, which is called the flue gas chemical recuperative cycle. This paper provides a meaningful review of the latest advancements in the flue gas chemical recuperative cycle system, focusing on its application in diverse gasification systems for organic matters such as methane, sludge, etc. Additionally, this paper reviews methods for the integration of flue gas gasification into energy conversion and utilization systems under the application scenarios of gas turbine flue gas, air combustion flue gas, and oxy-fuel combustion flue gas. Subsequently, in order to improve the conversion efficiency of the chemical recuperative cycle, the applications of emerging gasification technologies in the field of the flue gas recuperative cycle, such as microwave gasification, plasma gasification, etc., are briefly summarized, offering an in-depth analysis of the mechanisms by which new methods enhance the process. Finally, the prospects and challenges of the field are discussed, and a comprehensive outlook is provided to guide future research. Full article
(This article belongs to the Section B: Energy and Environment)
Show Figures

Figure 1

Figure 1
<p>Different research areas of the flue gas recuperative cycle.</p>
Full article ">Figure 2
<p>Clustered view of flue gas gasification keywords.</p>
Full article ">Figure 3
<p>Number of publications of related literature in various journals.</p>
Full article ">Figure 4
<p>Distribution of citations and publications from 1996 to 2024.</p>
Full article ">Figure 5
<p>Top 20 countries or regions in terms of documentation.</p>
Full article ">Figure 6
<p>Cooperation between China and major research countries.</p>
Full article ">Figure 7
<p>Chemically recuperated gas turbine concept [<a href="#B6-energies-18-00232" class="html-bibr">6</a>].</p>
Full article ">Figure 8
<p>Schematic diagram of the MR-CRGT [<a href="#B34-energies-18-00232" class="html-bibr">34</a>].</p>
Full article ">Figure 9
<p>(<b>a</b>) Flow chart of conventional biogas CHP system; (<b>b</b>) flow chart of biogas CHP system based on chemical recovery gas turbine cycle [<a href="#B36-energies-18-00232" class="html-bibr">36</a>].</p>
Full article ">Figure 10
<p>The proposed tri-generation model using methane fuel and biomass feedstock [<a href="#B38-energies-18-00232" class="html-bibr">38</a>].</p>
Full article ">Figure 11
<p>Schematic diagram of the stack gas–air MSW gasification and waste heat recovery system [<a href="#B9-energies-18-00232" class="html-bibr">9</a>].</p>
Full article ">Figure 12
<p>A process of MSW gasification by recycling hot BFG [<a href="#B42-energies-18-00232" class="html-bibr">42</a>].</p>
Full article ">Figure 13
<p>Configuration of complete BIGCC [<a href="#B14-energies-18-00232" class="html-bibr">14</a>].</p>
Full article ">Figure 14
<p>Distribution of citations and publications from 1999 to 2024.</p>
Full article ">Figure 15
<p>Difference in temperature distribution and direction of heat transfer between conventional heating and microwave heating. The arrows indicate the direction in which the heat is transferred. (<b>A</b>) Conventional heating: heat is transferred from the outside of the material inwards by conduction. Overheating can occur on the outside whist still maintaining a cooler inner region. (<b>B</b>) Microwave heating: MWs penetrate the material and heat volumetrically. Energy is then uniformly dissipated throughout the material [<a href="#B105-energies-18-00232" class="html-bibr">105</a>].</p>
Full article ">Figure 16
<p>Schematic diagram of CH<sub>4</sub>–CO<sub>2</sub> reforming reaction over Fe/SiC catalysts [<a href="#B104-energies-18-00232" class="html-bibr">104</a>].</p>
Full article ">Figure 17
<p>The process of H<sub>2</sub> generation in the steam–CO<sub>2</sub> mixed atmosphere [<a href="#B87-energies-18-00232" class="html-bibr">87</a>].</p>
Full article ">Figure 18
<p>Advantages of plasma technologies [<a href="#B110-energies-18-00232" class="html-bibr">110</a>].</p>
Full article ">
30 pages, 3092 KiB  
Review
Towards a Greener Future: Sustainable Innovations in the Extraction of Lavender (Lavandula spp.) Essential Oil
by Sara Hedayati, Mohammad Tarahi, Arghavan Madani, Seyed Mohammad Mazloomi and Mohammad Hashem Hashempur
Foods 2025, 14(1), 100; https://doi.org/10.3390/foods14010100 - 2 Jan 2025
Viewed by 1012
Abstract
Lavender is one of the most appreciated aromatic plants, with high economic value in food, cosmetics, perfumery, and pharmaceutical industries. Lavender essential oil (LEO) is known to have demonstrative antimicrobial, antioxidant, therapeutic, flavor and fragrance properties. Conventional extraction methods, e.g., steam distillation (SD) [...] Read more.
Lavender is one of the most appreciated aromatic plants, with high economic value in food, cosmetics, perfumery, and pharmaceutical industries. Lavender essential oil (LEO) is known to have demonstrative antimicrobial, antioxidant, therapeutic, flavor and fragrance properties. Conventional extraction methods, e.g., steam distillation (SD) and hydro-distillation (HD), have been traditionally employed to extract LEO. However, the low yield, high energy consumption, and long extraction time of conventional methods have prompted the introduction of novel extraction technologies. Some of these innovative approaches, such as ohmic-assisted, microwave-assisted, supercritical fluid, and subcritical water extraction approaches, are used as substitutes to conventional extraction methods. While other methods, e.g., sonication, pulsed electric field, and cold plasma, can be used as a pre-treatment that is preceded by conventional or emerging extraction technologies. These innovative approaches have a great significance in reducing the energy consumption, shortening the extraction time, and increasing the extraction yield and the quality of EOs. Therefore, they can be considered as sustainable extraction technologies. However, the scale-up of emerging technologies to an industrial level should also be investigated from the techno-economic points of view in future studies. Full article
Show Figures

Figure 1

Figure 1
<p>Photographs of four common lavender species: (<b>A</b>) <span class="html-italic">L. angustifolia</span>; (<b>B</b>) <span class="html-italic">L. latifolia</span>; (<b>C</b>) <span class="html-italic">L. stoechas</span>; and (<b>D</b>) <span class="html-italic">L. × intermedia</span>.</p>
Full article ">Figure 2
<p>A schematic diagram of the supercritical CO<sub>2</sub> extraction technique. The numbers 1, 2 and 3 indicate the stopping valves; adapted from Danh et al. [<a href="#B71-foods-14-00100" class="html-bibr">71</a>].</p>
Full article ">Figure 3
<p>A schematic diagram of the subcritical water extraction system; adapted from Díaz-Reinoso et al. [<a href="#B94-foods-14-00100" class="html-bibr">94</a>].</p>
Full article ">Figure 4
<p>A schematic diagram of the microwave-assisted steam distillation (MASD) system; adapted from Périno-Issartier et al. [<a href="#B108-foods-14-00100" class="html-bibr">108</a>].</p>
Full article ">Figure 5
<p>A schematic diagram of the dielectric barrier discharge (DBD) plasma system; adapted from Ucar et al. [<a href="#B127-foods-14-00100" class="html-bibr">127</a>].</p>
Full article ">Figure 6
<p>A schematic diagram of the ohmic-accelerated steam distillation (OASD) system; adapted from Gavahian and Chu [<a href="#B132-foods-14-00100" class="html-bibr">132</a>].</p>
Full article ">
12 pages, 1348 KiB  
Article
The Influence of Process Parameters on Hydrogen-Terminated Diamond and the Enhancement of Carrier Mobility
by Xingqiao Chen, Mingyang Yang, Yuanyuan Mu, Chengye Yang, Zhenglin Jia, Chaoping Liu, He Li, Nan Jiang, Kazuhito Nishimura, Liangchao Guo, Kuan W. A. Chee, Qilong Yuan, Xiaocheng Li and Hui Song
Materials 2025, 18(1), 112; https://doi.org/10.3390/ma18010112 - 30 Dec 2024
Viewed by 425
Abstract
With the development of diamond technology, its application in the field of electronics has become a new research hotspot. Hydrogen-terminated diamond has the electrical properties of P-type conduction due to the formation of two-dimensional hole gas (2DHG) on its surface. However, due to [...] Read more.
With the development of diamond technology, its application in the field of electronics has become a new research hotspot. Hydrogen-terminated diamond has the electrical properties of P-type conduction due to the formation of two-dimensional hole gas (2DHG) on its surface. However, due to various scattering mechanisms on the surface, its carrier mobility is limited to 50–200 cm2/(Vs). In this paper, the effects of process parameters (temperature, CH4 concentration, time) on the electrical properties of hydrogen-terminated diamond were studied by microwave plasma chemical vapor deposition (CVD) technology, and hydrogen-terminated diamond with a high carrier mobility was obtained. The results show that homoepitaxial growth of a diamond film on a diamond substrate can improve the carrier mobility. Hydrogen-terminated diamond with a high carrier mobility and low sheet resistance can be obtained by homoepitaxial growth of a high-quality diamond film on a diamond substrate with 4% CH4 concentration and hydrogen plasma treatment at 900 ℃ for 30 min. When the carrier concentration is 2.03 × 1012/cm2, the carrier mobility is 395 cm2/(Vs), and the sheet resistance is 7.82 kΩ/square, which greatly improves the electrical properties of hydrogen-terminated diamond. It can enhance the transmission characteristics of carriers in the conductive channel, and is expected to become a potential material for application in devices, providing a material choice for its application in the field of semiconductor devices. Full article
Show Figures

Figure 1

Figure 1
<p>(<b>a</b>) Raman spectra of hydrogen-terminated diamonds epitaxially grown at different CH<sub>4</sub> concentrations; (<b>b</b>) photoluminescence spectra of hydrogen-terminated diamonds and diamond substrates epitaxially grown at different CH<sub>4</sub> concentrations; (<b>c</b>) the ratio of [N-V]<sup>0</sup> and [N-V]<sup>−</sup> to the pl intensity of the diamond characteristic peak; and (<b>d</b>) homoepitaxial growth rate of the different samples.</p>
Full article ">Figure 2
<p>Surface roughness of hydrogen-terminated diamonds epitaxially grown at different CH<sub>4</sub> concentrations: (<b>a</b>) 1%; (<b>b</b>) 2%; (<b>c</b>) 3%; (<b>d</b>) 4%; (<b>e</b>) 5%; and (<b>f</b>) the relationship between a sample and roughness.</p>
Full article ">Figure 3
<p>Surface roughness of the homoepitaxial growth layer treated with hydrogen plasma at different times: (<b>a</b>) 15 min; (<b>b</b>) 30 min; (<b>c</b>) 45 min; and (<b>d</b>) the relationship between time and roughness.</p>
Full article ">Figure 4
<p>Electrical properties of hydrogen-terminated diamond under different conditions: (<b>a</b>) relationship between carrier mobility and carrier concentration and sample; (<b>b</b>) relationship between sheet resistance and sample; (<b>c</b>) relationship between carrier mobility and carrier concentration and hydrogen plasma treatment time; and (<b>d</b>) relationship between sheet resistance and hydrogen plasma treatment time.</p>
Full article ">Figure 5
<p>Surface roughness of hydrogen-terminated diamond at different hydrogen plasma treatment temperatures: (<b>a</b>) 600 °C; (<b>b</b>) 700 °C; (<b>c</b>) 800 °C; (<b>d</b>) 900 °C; (<b>e</b>) 1000 °C; and (<b>f</b>) the relationship between temperature and roughness.</p>
Full article ">Figure 6
<p>Electrical properties of hydrogen-terminated diamond with different hydrogen plasma treatment temperatures: (<b>a</b>) carrier mobility and carrier concentration; (<b>b</b>) sheet resistance.</p>
Full article ">Figure 7
<p>C 1s spectra and oxygen content of different diamonds: (<b>a</b>) diamond substrate; (<b>b</b>) hydrogen-terminated diamond prepared by hydrogen plasma treatment at 900 °C; (<b>c</b>) hydrogen-terminated diamond prepared by homoepitaxial growth of 4% CH<sub>4</sub>; and (<b>d</b>) the relationship between three different diamonds and surface oxygen content.</p>
Full article ">
16 pages, 4744 KiB  
Article
Research on the Production of Hydrogen Fluoride from Silicon Tetrafluoride Using 2.45 GHz Microwave Plasma
by Songlin Liu, Lianjun Shi, Guilan Liu, Wei Xiao and Huacheng Zhu
Processes 2025, 13(1), 4; https://doi.org/10.3390/pr13010004 - 24 Dec 2024
Viewed by 476
Abstract
Silicon tetrafluoride (SiF4), being a toxic gas, contains abundant fluorine and silicon resources. However, at present, the extraction of these resources from SiF4 remains a significant challenge for current technologies. Microwave plasma emerges as a promising technology with considerable potential [...] Read more.
Silicon tetrafluoride (SiF4), being a toxic gas, contains abundant fluorine and silicon resources. However, at present, the extraction of these resources from SiF4 remains a significant challenge for current technologies. Microwave plasma emerges as a promising technology with considerable potential in this area. Nevertheless, the majority of research endeavors concentrate on the silicon production through microwave plasma treatment of SiF4, while the resultant tail gas, rich in fluorine resources, is neglected and subsequently wasted. In this paper, a low-pressure microwave plasma is employed to process SiF4 and H2 for the one-step synthesis of hydrogen fluoride (HF). The microwave power reflection ratio, electron density, SF4 conversion rate, and produced HF concentration in varying microwave power levels and gas flow rates are obtained. The results demonstrate that all the processing parameters have a direct impact on the HF concentration. The maximum HF concentration of 11,200 ppm is achieved under the specific condition: an H2 flow rate of 2.5 sccm, a SiF4 flow rate of 2 sccm, and a microwave power level of 1100 W. Notably, this condition also results in the lowest energy cost. Moreover, the underlying reaction mechanism of the conversion from SiF4 to HF is thoroughly analyzed. This work presents fundamental process guidance for the production of HF using microwave plasma, facilitating the scalability of this technology in industry. Full article
(This article belongs to the Special Issue Microwave Applications in Chemistry and Industry)
Show Figures

Figure 1

Figure 1
<p>Microwave plasma experimental system for HF generation. (<b>a</b>) Schematic. (<b>b</b>) Photograph.</p>
Full article ">Figure 2
<p>Schematic of (<b>a</b>) 3D domain of the microwave-plasma interaction, (<b>b</b>) electron density distribution model, and (<b>c</b>) boundaries.</p>
Full article ">Figure 3
<p>Microwave power reflection ratio and electron density under different microwave power levels. (<b>a</b>,<b>b</b>) 400 W; (<b>c</b>,<b>d</b>) 510 W; (<b>e</b>,<b>f</b>) 670 W; (<b>g</b>,<b>h</b>) 820 W; (<b>i</b>,<b>j</b>) 1100 W.</p>
Full article ">Figure 3 Cont.
<p>Microwave power reflection ratio and electron density under different microwave power levels. (<b>a</b>,<b>b</b>) 400 W; (<b>c</b>,<b>d</b>) 510 W; (<b>e</b>,<b>f</b>) 670 W; (<b>g</b>,<b>h</b>) 820 W; (<b>i</b>,<b>j</b>) 1100 W.</p>
Full article ">Figure 4
<p>HF production and conversion rate of SiF<sub>4</sub> under different microwave power levels. (<b>a</b>,<b>b</b>) 400 W; (<b>c</b>,<b>d</b>) 510 W; (<b>e</b>,<b>f</b>) 670 W; (<b>g</b>,<b>h</b>) 820 W; (<b>i</b>,<b>j</b>) 1100 W.</p>
Full article ">Figure 4 Cont.
<p>HF production and conversion rate of SiF<sub>4</sub> under different microwave power levels. (<b>a</b>,<b>b</b>) 400 W; (<b>c</b>,<b>d</b>) 510 W; (<b>e</b>,<b>f</b>) 670 W; (<b>g</b>,<b>h</b>) 820 W; (<b>i</b>,<b>j</b>) 1100 W.</p>
Full article ">Figure 5
<p>Energy cost for producing HF under different microwave power. (<b>a</b>) 400 W; (<b>b</b>) 510 W; (<b>c</b>) 670 W; (<b>d</b>) 820 W; (<b>e</b>) 1100 W.</p>
Full article ">
20 pages, 9396 KiB  
Article
Characterization of the Plasma Generated by a Compact Theta Pinch
by Sagi Turiel, Alexander Gribov, Daniel Maler and Yakov E. Krasik
Plasma 2024, 7(4), 978-997; https://doi.org/10.3390/plasma7040053 - 20 Dec 2024
Viewed by 524
Abstract
Theta Pinch is one of the promising methods for the generation of hot and dense plasma. In this paper, we describe the results of experimental research on a small-scale Theta Pinch created with Helium or Hydrogen plasmas. Different plasma diagnostics, namely, optical, microwave [...] Read more.
Theta Pinch is one of the promising methods for the generation of hot and dense plasma. In this paper, we describe the results of experimental research on a small-scale Theta Pinch created with Helium or Hydrogen plasmas. Different plasma diagnostics, namely, optical, microwave cut-off, laser interferometry, visible spectroscopy, Thomson scattering, and Laser-Induced Fluorescence were used to characterize the time- and space-resolved evolution of the plasma parameters, and the specific features of these diagnostic results obtained are discussed. The measured plasma density and the electron and ion temperature evolution, obtained by these various diagnostic tools, agree to a satisfactory level. These methods will be applied for studies of the parameters of the plasma in the device that is being developed by the nT-Tao company towards fusion energy. Full article
Show Figures

Graphical abstract

Graphical abstract
Full article ">Figure 1
<p>The experimental setup used to produce a Theta Pinch with a single loop.</p>
Full article ">Figure 2
<p>Waveforms of the current for the 1 μF capacitor charged to 17 kV and discharged into the three-loop coil (black line) and two 0.44 μF capacitors connected in parallel, charged to 25 kV and discharged into a single-loop coil (red dashed line). The He gas pressure in the tube was 0.1 Pa.</p>
Full article ">Figure 3
<p>Three-loop Theta Pinch coil. (<b>a</b>) Waveforms of the discharge current at 2.7 kPa pressure when no plasma generation was obtained (black) and with the plasma generation at 0.4 kPa (red) pressure of He gas. (<b>b</b>) Energy deposited into the gas discharge vs. gas pressure for He (black squares) and H<sub>2</sub> (red dots).</p>
Full article ">Figure 4
<p>Single-loop Theta Pinch. (<b>a</b>) Waveforms of the discharge current obtained in the case of Helium gas at 0.1 Pa pressure when no plasma generation was obtained (black) and with plasma generation at 0.4 kPa (red) pressure of He gas. (<b>b</b>) Energy deposited into the gas discharge versus He (black squares) and H<sub>2</sub> (red dots) pressure.</p>
Full article ">Figure 5
<p>Axial view frame images of the light emission (<b>top row</b>) obtained at different times of plasma compression for a single-loop Theta Pinch at Hydrogen pressure of 63 Pa and at frame duration of 10 ns; transversal view frame images of light emission (<b>bottom row</b>) obtained at different times for the three-loops setup at Hydrogen pressure of 106 Pa and at frame duration of 10 ns.</p>
Full article ">Figure 6
<p>Typical waveforms of current (black) and photodiode light intensity (red) obtained for single-loop (<b>a</b>) and three-loop (<b>b</b>) setups for 63 Pa Hydrogen.</p>
Full article ">Figure 7
<p>Lee model current (solid black) compared with the measured current (dashed black) for single-loop (<b>a</b>) and three-loop (<b>b</b>) setups and calculated shock (red) and piston (blue) radii during initial compression. He gas pressure is 63 Pa.</p>
Full article ">Figure 8
<p>Microwave cutoff setup for a three-loop Theta Pinch setup: (1) 32 V DC source, (2) the klystron and antenna (70 GHz), (3) receiving antenna with the Schottky diode, (4) photodiode, (5) Pierson current monitor. Microwaves are marked as green arrows.</p>
Full article ">Figure 9
<p>Typical waveforms of the discharge current, light emission, and transmitted microwave intensity (<b>a</b>) obtained for Helium at 63 Pa pressure. The transmitted microwave intensity for Hydrogen (<b>b</b>) and Helium (<b>c</b>) plasma experiments at different gas pressures. All results are for the three-loop setup.</p>
Full article ">Figure 10
<p>Michelson interferometer set up for average plasma density measurements for a three-loop Theta Pinch experiment. (1) Laser; (2) beam splitter; (3) and (4) mirrors; (5) bandpass filter matching the laser wavelength; (6) photodiode; (7) ND filter.</p>
Full article ">Figure 11
<p>(<b>a</b>) Interference waveform measured on a ms timescale. (<b>b</b>) Interference waveform measured on a 100 μs timescale. (<b>c</b>) Electron density (black) and discharge current in relative units (red) for 53 Pa Hydrogen plasma and a three-loop setup.</p>
Full article ">Figure 12
<p>Electron density evolution at different pressures of Hydrogen plasma using the green laser (<b>a</b>), red laser (<b>b</b>), and (<b>c</b>) Helium plasma (green laser) for a three-loop Theta Pinch setup.</p>
Full article ">Figure 13
<p>Spectroscopy setup. A single-loop setup.</p>
Full article ">Figure 14
<p>(<b>a</b>) Ion temperature, (<b>b</b>) electron density, and (<b>c</b>) electron temperature calculated for Hydrogen plasma at various gas pressures for the three-loops setup.</p>
Full article ">Figure 15
<p>Electron temperatures estimated 4 and 5 μs after the start of the current using a Boltzmann plot.</p>
Full article ">Figure 16
<p>Electron density calculated using the three relations involving the forbidden–allowed transition of the 447.1 spectral line of the He I atom.</p>
Full article ">Figure 17
<p>Setup for Thomson scattering experiment. Single-loop setup.</p>
Full article ">Figure 18
<p>(<b>a</b>) Thomson scattering spectrum measured for 53 Pa Hydrogen gas pressure at the time of plasma compression with ~20 eV ion temperature (black) compared to the numerical SDF with the same ion temperature for different electron temperatures and densities. (<b>b</b>) The central spectral feature measured with the high-resolution spectrometer at the same time and same gas pressure (black) compared to the SDF calculated for <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>n</mi> </mrow> <mrow> <mi>e</mi> </mrow> </msub> <mo>=</mo> <mn>5</mn> <mo>⋅</mo> <msup> <mrow> <mn>10</mn> </mrow> <mrow> <mn>16</mn> </mrow> </msup> <mo> </mo> <mi mathvariant="normal">c</mi> <msup> <mrow> <mi mathvariant="normal">m</mi> </mrow> <mrow> <mo>−</mo> <mn>3</mn> </mrow> </msup> </mrow> </semantics></math> for different <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>T</mi> </mrow> <mrow> <mi>e</mi> </mrow> </msub> </mrow> </semantics></math>.</p>
Full article ">Figure 19
<p>Experimental setup for Helium LIF measurements. Single-loop setup.</p>
Full article ">Figure 20
<p>Dependence of the LIF amplitude measured at 100 μs and 60 μs after the plasma compression vs. the Q-switch delay time.</p>
Full article ">Figure 21
<p>LIF spectral line profiles measured at 60 μs (<b>a</b>) and 100 μs (<b>b</b>) after the plasma compression and at ~275 ns, ~300 ns, and ~375 ns before the plasma compression (<b>c</b>).</p>
Full article ">Figure 22
<p>LIF intensity of <math display="inline"><semantics> <mrow> <msub> <mrow> <mi>H</mi> </mrow> <mrow> <mi>α</mi> </mrow> </msub> </mrow> </semantics></math> vs. the wavelength of the dye laser at different time delays relative to the first plasma compression: (<b>a</b>) 300 ns prior to plasma compression, (<b>b</b>) at the time of the plasma compression, and (<b>c</b>) 40 μs after the plasma.</p>
Full article ">
10 pages, 854 KiB  
Article
Differentiation of Insect Flours by Elemental Analysis and Chemometrics: A Study Using Inductively Coupled Plasma Mass Spectrometry (ICP-MS)
by Mattia Montanaro, Alessandra Biancolillo, Angelo Antonio D’Archivio and Martina Foschi
Molecules 2024, 29(24), 5878; https://doi.org/10.3390/molecules29245878 - 12 Dec 2024
Viewed by 715
Abstract
Background: This study aimed to validate a method for characterizing and quantifying the multi-elemental profiles of different insect flours to enable their distinction, identification, and quality assessment. The focus was on three insect species: cricket (Acheta domesticus), buffalo worm (Alphitobius [...] Read more.
Background: This study aimed to validate a method for characterizing and quantifying the multi-elemental profiles of different insect flours to enable their distinction, identification, and quality assessment. The focus was on three insect species: cricket (Acheta domesticus), buffalo worm (Alphitobius diaperinus), and mealworm (Tenebrio molitor). Methods: Mealworms were powdered in the laboratory through mechanical processing. Sample analysis involved acid digestion using a microwave digester, followed by profiling with Inductively Coupled Plasma Mass Spectrometry (ICP-MS). This technique enabled rapid, multi-elemental analysis at trace levels. Chemometric methods, including Principal Component Analysis (PCA) for exploratory analysis, Covariance Selection-Linear Discriminant Analysis (CovSel-LDA), alongside forward stepwise LDA classification methods, were applied and compared. Results: ICP-MS accurately detected elements at micro trace levels. Both classification models, based on different variable selection methods and externally validated on a test set comprising 45% of the available samples, proved effective in classifying samples based on slightly different pools of trace elements. CovSel-LDA selected Mg and Se, whereas the stepwise-LDA focused on Mg, K, and Mn. Conclusions: the validated methods demonstrated high accuracy and generalizability, supporting their potential use in food industry applications. This model could assist in quality control, facilitating the introduction of insect-based flour into European and international markets as novel foods. Full article
Show Figures

Figure 1

Figure 1
<p>Biplot with the first two principal components. The percentage in brackets is the variance explained by each PC. Legend: Black dots represent the diverse quantified elements. Green downward triangles depict buffalo worms; yellow circles for house crickets; and red squares represent mealworms.</p>
Full article ">Figure 2
<p>Projection of samples (filled and empty symbols refer to training and test samples, respectively) onto the canonical variates (CVs) obtained by the CovSel-LDA model.</p>
Full article ">
Back to TopTop