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19 pages, 3234 KiB  
Article
Highly Efficient and Environmentally Friendly Walnut Shell Carbon for the Removal of Ciprofloxacin, Diclofenac, and Sulfamethoxazole from Aqueous Solutions and Real Wastewater
by Seda Tunay, Rabia Koklu and Mustafa Imamoglu
Processes 2024, 12(12), 2766; https://doi.org/10.3390/pr12122766 - 5 Dec 2024
Viewed by 452
Abstract
The objective of this study is to assess the efficacy of walnut shell-derived activated carbon with phosphoric acid (WSAC) in the removal of ciprofloxacin (CIP), diclofenac (DC), and sulfamethoxazole (SMX) from aqueous solutions and real wastewater. WSAC was characterized using various analytical techniques [...] Read more.
The objective of this study is to assess the efficacy of walnut shell-derived activated carbon with phosphoric acid (WSAC) in the removal of ciprofloxacin (CIP), diclofenac (DC), and sulfamethoxazole (SMX) from aqueous solutions and real wastewater. WSAC was characterized using various analytical techniques such as specific surface area and pore size distribution determination, elemental analysis, SEM images, and FT-IR spectroscopy. The BET-specific surface area of WSAC was determined to be 1428 m2 g−1. The surface is characterized by the presence of irregular pits of varying dimensions and shapes. The adsorption of SMX, CIP, and DC from aqueous solutions using WSAC was tested under various parameters, including contact time, adsorbent dosage, initial concentration, pH, and temperature. The adsorption of SMX, CIP, and DC was found to be in accordance with the Langmuir isotherm model, which suggests that monomolecular adsorption is the predominant mechanism. The maximum adsorption capacities of WSAC towards SMX, CIP, and DC were calculated to be 476.2, 185.2, and 135.1 mg g−1, respectively. The adsorption of SMX, CIP, and DC were found to be consistent with the pseudo-second-order model. Thermodynamic analyses demonstrated the spontaneous and endothermic nature of SMX, CIP, and DC adsorption onto WSAC. The adsorption performances of SMX, CIP, and DC on WSAC were found to be 60.2%, 77.4%, and 74.2%, respectively in the effluent from the municipal wastewater treatment plant. In conclusion, WSAC may be regarded as a readily available, eco-friendly, and efficient substance for the extraction of SMX, CIP, and DC from wastewater and aqueous solutions. Full article
(This article belongs to the Section Chemical Processes and Systems)
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<p>SEM images of WSAC at various magnification: (<b>a</b>) 1000 and (<b>b</b>) 5000.</p>
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<p>N<sub>2</sub> adsorption/desorption isotherms of WSAC.</p>
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<p>Pore size distribution of WSAC.</p>
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<p>FT-IR spectrum of WSAC.</p>
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<p>The effect of contact time on the adsorption of SMX, CIP, and DC (<b>A</b>); the effect of WSAC dosage on the adsorption of CIP, DC (<b>B1</b>) and SMX (<b>B2</b>); the effect of initial concentration on the adsorption of CIP, DC (<b>C1</b>) and SMX (<b>C2</b>); the effect of initial pH on the adsorption of SMX, CIP, and DC (<b>D</b>); the effect of temperature on the adsorption of SMX, CIP, and DC (<b>E</b>).</p>
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<p>Freundlich, Langmuir, Dubinin–Radushkevich and Temkin models for SMX, CIP, and DC adsorption onto WSAC.</p>
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<p>Adsorption of SMX, CIP, and DC from solutions (<b>A</b>) and wastewater (<b>B</b>) by WSAC.</p>
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<p>Desorption (<b>A</b>) and recyclability (<b>B</b>) of WSAC for SMX, DC, and CIP.</p>
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17 pages, 3796 KiB  
Article
FastQAFPN-YOLOv8s-Based Method for Rapid and Lightweight Detection of Walnut Unseparated Material
by Junqiu Li, Jiayi Wang, Dexiao Kong, Qinghui Zhang and Zhenping Qiang
J. Imaging 2024, 10(12), 309; https://doi.org/10.3390/jimaging10120309 - 2 Dec 2024
Viewed by 533
Abstract
Walnuts possess significant nutritional and economic value. Fast and accurate sorting of shells and kernels will enhance the efficiency of automated production. Therefore, we propose a FastQAFPN-YOLOv8s object detection network to achieve rapid and precise detection of unsorted materials. The method uses lightweight [...] Read more.
Walnuts possess significant nutritional and economic value. Fast and accurate sorting of shells and kernels will enhance the efficiency of automated production. Therefore, we propose a FastQAFPN-YOLOv8s object detection network to achieve rapid and precise detection of unsorted materials. The method uses lightweight Pconv (Partial Convolution) operators to build the FasterNextBlock structure, which serves as the backbone feature extractor for the Fasternet feature extraction network. The ECIoU loss function, combining EIoU (Efficient-IoU) and CIoU (Complete-IoU), speeds up the adjustment of the prediction frame and the network regression. In the Neck section of the network, the QAFPN feature fusion extraction network is proposed to replace the PAN-FPN (Path Aggregation Network—Feature Pyramid Network) in YOLOv8s with a Rep-PAN structure based on the QARepNext reparameterization framework for feature fusion extraction to strike a balance between network performance and inference speed. To validate the method, we built a three-axis mobile sorting device and created a dataset of 3000 images of walnuts after shell removal for experiments. The results show that the improved network contains 6071008 parameters, a training time of 2.49 h, a model size of 12.3 MB, an mAP (Mean Average Precision) of 94.5%, and a frame rate of 52.1 FPS. Compared with the original model, the number of parameters decreased by 45.5%, with training time reduced by 32.7%, the model size shrunk by 45.3%, and frame rate improved by 40.8%. However, some accuracy is sacrificed due to the lightweight design, resulting in a 1.2% decrease in mAP. The network reduces the model size by 59.7 MB and 23.9 MB compared to YOLOv7 and YOLOv6, respectively, and improves the frame rate by 15.67 fps and 22.55 fps, respectively. The average confidence and mAP show minimal changes compared to YOLOv7 and improved by 4.2% and 2.4% compared to YOLOv6, respectively. The FastQAFPN-YOLOv8s detection method effectively reduces model size while maintaining recognition accuracy. Full article
(This article belongs to the Section Computer Vision and Pattern Recognition)
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<p>Sample images of the dataset.</p>
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<p>Experimental platform preparation. (<b>a</b>) Experimental platform (<b>b</b>) Field of view of the camera.</p>
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<p>YOLOv8s improvement process diagram.</p>
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<p>YOLOv8s specific improvement layer.</p>
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<p>FasterNext structure construction.</p>
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<p>QAFPN structure construction.</p>
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<p>Comparison of different loss functions.</p>
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<p>Graph of recognition results of different models.</p>
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22 pages, 7889 KiB  
Article
Magnesium Bicarbonate–Walnut Shell Dual-Template Synthesis of Multifunctional Layered Porous Carbon for Enhanced Adsorption of Aqueous Chlorinated Organic Compounds
by Juanxue Kang, Xiaoli Bai, Junyang Leng, Yaxuan Lou, Daomei Chen, Liang Jiang and Jiaqiang Wang
Int. J. Mol. Sci. 2024, 25(21), 11761; https://doi.org/10.3390/ijms252111761 - 1 Nov 2024
Viewed by 596
Abstract
Chloride ions readily react with organic matter and other ions, resulting in the formation of disinfection by-products (DBPs) that exhibit heightened levels of toxicity, carcinogenicity, and mutagenicity. This study creatively employed waste walnut shells as self-templates and low-cost magnesium bicarbonate as a rigid [...] Read more.
Chloride ions readily react with organic matter and other ions, resulting in the formation of disinfection by-products (DBPs) that exhibit heightened levels of toxicity, carcinogenicity, and mutagenicity. This study creatively employed waste walnut shells as self-templates and low-cost magnesium bicarbonate as a rigid template to successfully synthesize multifunctional porous carbon derived from walnut shells. Employing a series of characterization techniques, it was ascertained that the porous carbon material (WSC/Mg) synthesized via the dual-template method exhibited a distinct layered microscopic surface structure, with a predominance of C and O elements on the surface. The material displayed a high degree of graphitization, significant specific surface area, and abundant oxygen-containing surface functional groups. The incorporation of magnesium bicarbonate as a hard template improved the structure of the walnut shell porous carbon, resulting in a significant enhancement in mass transfer efficiency for the target product on the adsorbent and a substantial improvement in removal efficiency. In comparison with walnut shell-derived carbon using only self-templating, WSC/Mg exhibited a 17.26-fold increase in adsorption capacity for 2,4-dichlorophenol. Furthermore, even after four adsorption–desorption cycles, WSC/Mg-12 maintained an adsorption efficiency above 90%. It is remarkable that WSC/Mg-12 demonstrated exceptional resistance to interference from natural organic matter and pH variations. Moreover, the adsorbed saturated WSC/Mg-12 effectively treated real coke wastewater, resulting in an 80% color removal rate, 20% COD removal rate, and 15% ammonia nitrogen removal rate. In conclusion, this study presents an innovative approach for cost-effective and versatile porous carbon materials with extensive applications in water environment purification and biomass utilization. Full article
(This article belongs to the Section Materials Science)
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<p>SEM images of (<b>a</b>) WSC; (<b>b</b>) WSC/Mg-21; (<b>c</b>) WSC/Mg-11; (<b>d</b>,<b>e</b>) WSC/Mg-12; and (<b>f</b>) WSC/Mg-13. (<b>g</b>) Element mapping of WSC/Mg-12.</p>
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<p>(<b>a</b>) FT-IR and (<b>b</b>) Raman spectra of WSC, WSC/Mg-21, WSC/Mg-11, WSC/Mg-12, and WSC/Mg-13.</p>
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<p>(<b>a</b>) N<sub>2</sub> adsorption–desorption curves; (<b>b</b>) pore size distribution of WSC, WSC/Mg-21, WSC/Mg-11, WSC/Mg-12, and WSC/Mg-13.</p>
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<p>(<b>a</b>) XPS; (<b>b</b>) C1s of WSC; (<b>c</b>) C1s of WSC/Mg-21; (<b>d</b>) C1s of WSC/Mg-11; (<b>e</b>) C1s of WSC/Mg-12; (<b>f</b>) C1s of WSC/Mg-13.</p>
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<p>(<b>a</b>) The effect of different materials; (<b>b</b>) the effect of dosage in 2,4-DCP on WSC/Mg-12.</p>
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<p>(<b>a</b>) The relationship between the duration of adsorption and the amount of adsorption; (<b>b</b>) pseudo-first order model; (<b>c</b>) pseudo-second order model; (<b>d</b>) intra-particle diffusion model of WSC/Mg-12.</p>
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<p>Adsorption isothermal models of WSC/Mg-12: (<b>a</b>) Langmuir; (<b>b</b>) Freundlich; (<b>c</b>) Temkin; (<b>d</b>) Sips.</p>
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<p>(<b>a</b>) Raman spectra, (<b>b</b>) FT-IR spectra, and (<b>c</b>) XPS of WSC-12 (used); (<b>d</b>) C1s, (<b>e</b>) O1s, and (<b>f</b>) Cl2p of WSC-12 (used).</p>
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<p>(<b>a</b>) 10,000× and (<b>b</b>) 100,000× SEM images of WSC-12 (used); (<b>c</b>) mapping of WSC-12 (used).</p>
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<p>Schematic illustration of possible adsorption mechanism.</p>
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<p>Adsorption of 2,4-DCP in different water samples.</p>
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<p>Recyclability of WSC/Mg-12.</p>
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<p>Comparison of coking wastewater pre-adsorption and post-adsorption.</p>
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<p>Schematic representation of WSC/Mg preparation procedure.</p>
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19 pages, 4442 KiB  
Article
Phytotoxicity Assessment of Agro-Industrial Waste and Its Biochar: Germination Bioassay in Four Horticultural Species
by Romina Zabaleta, Eliana Sánchez, Ana Laura Navas, Viviana Fernández, Anabel Fernandez, Daniela Zalazar-García, María Paula Fabani, Germán Mazza and Rosa Rodriguez
Agronomy 2024, 14(11), 2573; https://doi.org/10.3390/agronomy14112573 - 1 Nov 2024
Viewed by 664
Abstract
This study investigated the phytotoxicity of agro-industrial wastes (almond, walnut, pistachio and peanut shells, asparagus spears, and brewer’s spent grain) and their biochar through germination bioassays in several horticultural species: green pea, lettuce, radish, and arugula. Biowaste was pyrolyzed under controlled conditions to [...] Read more.
This study investigated the phytotoxicity of agro-industrial wastes (almond, walnut, pistachio and peanut shells, asparagus spears, and brewer’s spent grain) and their biochar through germination bioassays in several horticultural species: green pea, lettuce, radish, and arugula. Biowaste was pyrolyzed under controlled conditions to produce biochar, and both biowaste and biochar were characterized. Germination bioassay was conducted using seeds exposed to different dilutions of aqueous extract of biowaste and their biochar (0, 50, and 100%). Germination percentage, seed vigor, germination index, and root and aerial lengths were evaluated. The results showed that the phytotoxicity of the biowaste was significantly different to that of its biochar. The biochar obtained demonstrated changing effects on germination and seedling growth. In particular, biochar extracts from spent brewers grains, walnut shells, and pistachio shells showed 5–14% increases in seed vigor and root and aerial length. Furthermore, the response of different species to both agro-industrial waste and biochar revealed species-specific sensitivity. Seeds of lettuce and arugula species were more sensitive to aqueous extracts than radish and green peas. This knowledge not only elucidates the behavior of agro-industrial waste-based biochar in the early stage of plant development but also provides valuable insights regarding phytotoxicity, seed sensitivity, and the variables involved in germination. Full article
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<p>Logic diagram, a methodological scheme of the germination bioassay in horticultural species: evaluation of biowaste and biochar.</p>
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<p>Biowastes: (<b>a</b>) Alm, (<b>b</b>) Wal, (<b>c</b>) Pea, (<b>d</b>) Pis, (<b>e</b>) Asp, and (<b>f</b>) Bre.</p>
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<p>Biochars: (<b>a</b>) AlmB, (<b>b</b>) WalB, (<b>c</b>) PeaB, (<b>d</b>) PisB, (<b>e</b>) AspB, and (<b>f</b>) BreB.</p>
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<p>Photographs taken at the end of the Petri dish assay. Horticultural seeds emerging in control extract: (<b>a</b>) <span class="html-italic">Lactuca sativa</span>, (<b>b</b>) <span class="html-italic">Eruca sativa</span>, (<b>c</b>) <span class="html-italic">Raphanus sativus</span>, and (<b>d</b>) <span class="html-italic">Pisum sativum</span>.</p>
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<p>Relationships between biomass and biochar types and control and their influence of variables (GI, GP, SV, AL, and RL) with discriminatory potential through a multivariate statistical procedure, such as linear discriminant analysis (LDA).</p>
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<p>Relationships between types of seeds and their influence on variables with discriminatory potential through a multivariate statistical procedure, such as linear discriminant analysis (LDA). GI (germination index), GP (germination percentage), SV (seed vigor), AL (aerial length) and RL (root length).</p>
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15 pages, 3368 KiB  
Article
Study on the Influence of Walnut Shell Coarse Particles on the Slurry Permeation and the Air Tightness of Filter Cake
by Qi Dong, Tao Liu, Yuan Wang, Sijin Liu and Letian Wen
Materials 2024, 17(21), 5186; https://doi.org/10.3390/ma17215186 - 24 Oct 2024
Viewed by 442
Abstract
Slurry shields rely on the formation of a compact filter cake to maintain excavation face stability and ensure construction safety. In strata with high permeability, significant slurry loss occurs, making filter cake formation and air tightness maintenance challenging. In this study, light organic [...] Read more.
Slurry shields rely on the formation of a compact filter cake to maintain excavation face stability and ensure construction safety. In strata with high permeability, significant slurry loss occurs, making filter cake formation and air tightness maintenance challenging. In this study, light organic walnut shell was selected as an additive coarse particle material for slurry. Slurries incorporating two types of coarse particles, sand and walnut shell, were prepared, and tests on slurry permeation and air tightness of the filter cake were conducted in three different strata. The results indicate that the addition of coarse particles effectively improves filter cake formation and air tightness in high-permeability strata. It is essential to use graded particles in highly permeable strata, with controlled maximum and minimum particle sizes. As the content of coarse particles increases, the air tightness of the filter cake initially increases and then decreases. Notably, the air tightness of filter cakes containing walnut shell is superior to those containing sand. Replacing sand with walnut shell as a slurry plugging material enhances filter cake quality in high-permeability strata. For highly permeable strata with a permeability coefficient greater than 1.0 × 10−3 m/s, an addition of 30 g/L to 40 g/L is recommended. Full article
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<p>Test system of slurry permeation and filter cake air tightness.</p>
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<p>The combination type of permeation band and filter cake.</p>
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<p>The bridging effect of coarse particles with different gradations in slurry.</p>
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<p>Infiltration flow rate curves of slurry in S3 stratums.</p>
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<p>Infiltration flow volume of forming filter cake under varied permeability strata and coarse particle content.</p>
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<p>The failure morphology of filter cake in high air pressure.</p>
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<p>The permeation flow rate curve of the filter cake during air tightness process.</p>
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<p>The air tightness pressure of the filter cake under varied permeability strata and coarse particle content.</p>
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<p>The form of failure of filter cake air tightness in constant air pressure.</p>
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<p>Flow volume through the filter cake under constant air pressure with varied coarse particle content.</p>
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<p>Three stages of air tightness of filter cake.</p>
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<p>The air tightness time of the filter cake under varied permeability strata and coarse particle content.</p>
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14 pages, 4192 KiB  
Article
Nutshell Materials as a Potential Eco-Friendly Biosorbent for the Effective Extraction of UV Filters and Parabens from Water Samples
by Izabela Narloch, Grażyna Wejnerowska and Przemysław Kosobucki
Materials 2024, 17(20), 5128; https://doi.org/10.3390/ma17205128 - 21 Oct 2024
Viewed by 566
Abstract
UV filters and parabens, as ingredients of cosmetics, are commonly occurring water pollutants. In our work, nutshells were used as biosorbents in the developed analytical procedure for the determination of UV filters and parabens in water samples. The shells obtained from walnuts, hazelnuts, [...] Read more.
UV filters and parabens, as ingredients of cosmetics, are commonly occurring water pollutants. In our work, nutshells were used as biosorbents in the developed analytical procedure for the determination of UV filters and parabens in water samples. The shells obtained from walnuts, hazelnuts, peanuts and pistachios were applied as biosorbents. The proposed analytical method can be used as a powerful alternative to other methods for the analysis of UV filters and parabens in water samples. A method of carrying out the sorption step and its parameters, i.e., the effect of time, pH, and salt addition, was developed. A method for the desorption of analytes was also developed, in which the type and volume of solvent, and the desorption time, were established. The recoveries were in the range of 59–117% for benzophenones and lower recoveries from 14 to 75% for parabens. The results showed that nutshells can be used as low-cost, efficient and eco-friendly biosorbents for the determination of parabens and UV filters in water samples. These materials can be used as a ‘greener’ replacement for the commercially available adsorbents for the extraction of cosmetic ingredients from the environment. Full article
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<p>Scheme of the proposed method.</p>
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<p>FT-IR spectrum of the walnut shells.</p>
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<p>SEM images of (<b>a</b>) walnut shells; (<b>b</b>) walnut shells after adsorption of analytes; (<b>c</b>) peanut shells; (<b>d</b>) peanut shells after adsorption of analytes.</p>
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<p>A bar graph for the optimization of (<b>a</b>) biosorbent mass: 10 mL of sample, pH 7, 20 min; (<b>b</b>) extraction time: 10 mL of sample, pH 7, biosorbent mass 200 mg; (<b>c</b>) pH solution: 10 mL of sample, 10 min, biosorbent mass 200 mg; (<b>d</b>) salt addition: 10 mL of sample, pH 4, 10 min, biosorbent mass 200 mg. For all optimization tests, the desorption step was performed with 1 × 1500 µL of ACN for 15 min.</p>
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<p>A bar graph for the optimization of the desorption condition: (<b>a</b>) the kind of desorption solvent: 1 × 1500 µL of solvent, 15 min; (<b>b</b>) the volume of solvent and number of cycles: desorption with ACN/OE, 15 min; (<b>c</b>) desorption time: 2 × 750 µL of ACN/OE; (<b>d</b>) biosorbent size: desorption with 2 × 750 µL of ACN/OE, 5 min. For all optimization tests, the sorption step was performed with 200 mg of biosorbent and 10 mL of sample, pH 4, 20% NaCl for 10 min.</p>
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<p>An assessment of greenness of the proposed sample preparation method, obtained by using the AGREEprep tool.</p>
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11 pages, 2599 KiB  
Article
Obtaining Lignin from Nutshells under Mild Extraction Conditions and Its Use as a Biostimulant in Tomato Seedlings
by José Alejandro Díaz-Elizondo, Azrrael Ayala-Velazco, Adalberto Benavides-Mendoza, Francisco Javier Enriquez-Medrano and Julia Medrano-Macías
Horticulturae 2024, 10(10), 1079; https://doi.org/10.3390/horticulturae10101079 - 9 Oct 2024
Viewed by 1481
Abstract
Biostimulants are an important alternative to improve and promote higher efficiency in cropping systems. Although the biostimulant industry has been developing for several years, there are still areas of opportunity for new sources of biostimulants as well as new ecofriendly extraction techniques that [...] Read more.
Biostimulants are an important alternative to improve and promote higher efficiency in cropping systems. Although the biostimulant industry has been developing for several years, there are still areas of opportunity for new sources of biostimulants as well as new ecofriendly extraction techniques that allow for a circular economy and the reuse of waste. Lignin is a heteropolymer that constitutes about 40% of the plant cell wall. A great source of lignin is agrowastes, giving it added value. Recently, its use has been tested in agronomy as a carrier of nutrients and pesticides. Walnuts are produced on a large scale in Northern Mexico, and the shell represents between 15 and 40% of its total weight. However, to obtain this biopolymer, to date, non-environmentally friendly techniques have been used; for this reason, it is necessary to find extraction alternatives to make this proposal sustainable. In this work, the obtaining and characterization of lignin through mild extraction conditions from nutshells and its evaluation as a biostimulant on the growth of tomato seedlings are reported. Lignin was extracted by hydrolysis with a mixture of acetic acid and distilled water (65:35 v/v). The results showed that it was possible to obtain 15% (w/w) lignin using mild solvents, evidenced by thermogravimetric analysis (TGA), proton magnetic nuclear resonance (H-RMN), and infrared (IR). Subsequently, lignin solutions were prepared at different concentrations, 0, 10, 50, and 100 ppm, and applied via foliar weekly to tomato seedlings. A greater fresh weight of the stem was found with 10 and 50 ppm, and the height and the fresh biomass increased with the three concentrations (10, 50, and 100 ppm), concluding that lignin extracted from nutshells using mild conditions can act as a plant biostimulant. Full article
(This article belongs to the Special Issue Application of Plant Biostimulants in Horticultural Crops)
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<p>Process of extraction and purification of lignin from nutshells.</p>
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<p>1H-NMR spectrum of the lignin from literature (<b>a</b>) Xu et al. [<a href="#B17-horticulturae-10-01079" class="html-bibr">17</a>] and (<b>b</b>) 1H-NMR spectrum of the lignin sample extracted from nutshells.</p>
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<p>FTIR spectrum of lignin extracted from the nutshells.</p>
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<p>SEM micrographs of lignin obtained from nutshells.</p>
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<p>EDS spectrum of lignin obtained from nutshells.</p>
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<p>Particle size distribution of lignin obtained from nutshells.</p>
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16 pages, 4027 KiB  
Article
Walnut Shell Biomass Triggered Formation of Fe3C-Biochar Composite for Removal of Diclofenac by Activating Percarbonate
by Na Zhang, Yudong Huo, Chun Pei, Ying Zhang, Lijie Xu and Lu Gan
Catalysts 2024, 14(10), 687; https://doi.org/10.3390/catal14100687 - 3 Oct 2024
Viewed by 1096
Abstract
Percarbonate (SPC) as a promising substitute for liquid H2O2 has many advantages in the application of in situ chemical oxidation (ISCO). Developing efficient, cost effective and environmentally friendly catalysts for SPC activation plays the key role in promoting the development [...] Read more.
Percarbonate (SPC) as a promising substitute for liquid H2O2 has many advantages in the application of in situ chemical oxidation (ISCO). Developing efficient, cost effective and environmentally friendly catalysts for SPC activation plays the key role in promoting the development of SPC-based ISCO. Herein, the walnut shell biomass was combined with ferric nitrate for the catalytic synthesis of Fe3C@biochar composite (Fe3C@WSB), which demonstrated high efficiency in activating SPC for the removal of diclofenac (DCF). The Fe3C showed average crystallite size of 32.6 nm and the composite Fe3C@WSB demonstrated strong adsorptivity. The prepared Fe3C@WSB could activate both SPC and H2O2 with high efficiency at ca. pH 3 with extremely low leaching of iron, while in a weak acidic condition, higher efficiency of DCF removal was obtained in the Fe3C@WSB/SPC process than in the Fe3C@WSB/H2O2 process. Moreover, the Fe3C@WSB/SPC and Fe3C@WSB/H2O2 processes did not show significant differences when supplied with varying amounts of catalyst or oxidant, but the Fe3C@WSB/SPC process exhibited stronger capability in dealing with relatively highly concentrated DCF solution. Based on quenching experiments and electron spin resonance (ESR) analysis, heterogeneous activation of SPC was assumed as the dominant route for DCF degradation, and both the oxidation by radicals, including •OH, •O2 and CO3•−, combined with electron transfer pathway contributed to DCF degradation in the Fe3C@WSB/SPC process. The cycling experiment results also revealed the stability of Fe3C@WSB. This work may cast some light on the development of efficient catalysts for the activation of SPC. Full article
(This article belongs to the Special Issue Advances in Catalytic Conversion of Biomass)
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<p>The XRD spectra of Fe<sub>3</sub>C@WSB.</p>
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<p>The N<sub>2</sub> adsorption–desorption curves and pore size distribution of Fe<sub>3</sub>C@WSB.</p>
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<p>SEM images of (<b>a</b>) WS-derived biochar and (<b>b</b>) Fe<sub>3</sub>C@WSB; (<b>c</b>) the atomic ratio of different elements on Fe<sub>3</sub>C@WSB surface; EDS mapping of (<b>d</b>) Fe, (<b>e</b>) C, and (<b>f</b>) O on the surface of Fe<sub>3</sub>C@WSB; (<b>g</b>,<b>h</b>) the TEM images of Fe<sub>3</sub>C@WSB.</p>
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<p>(<b>a</b>) The XPS survey spectra and (<b>b</b>) C 1s and (<b>c</b>) Fe 2p spectra of fresh Fe<sub>3</sub>C@WSB.</p>
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<p>The adsorption kinetics of DCF on Fe<sub>3</sub>C@WSB under different initial pH conditons (reaction conditions: [DCF]<sub>0</sub> = 0.02 mM, catalyst dosage 0.1 g/L).</p>
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<p>The removal kinetics of DCF in (<b>a</b>) Fe<sub>3</sub>C@WSB/SPC and (<b>b</b>) Fe<sub>3</sub>C@WSB/H<sub>2</sub>O<sub>2</sub> processes under different initial pH conditions; the corresponding consumption of H<sub>2</sub>O<sub>2</sub> in (<b>c</b>) Fe<sub>3</sub>C@WSB/SPC and (<b>d</b>) Fe<sub>3</sub>C@WSB/H<sub>2</sub>O<sub>2</sub> processes (reaction conditions: [DCF]<sub>0</sub> = 0.02 mM, catalyst dosage 0.1 g/L, [H<sub>2</sub>O<sub>2</sub>]<sub>0</sub> = 1.5 mM, [SPC]<sub>0</sub> = 1.0 mM).</p>
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<p>The leaching amount of Fe<sup>2+</sup> and total iron after the reaction in Fe<sub>3</sub>C@WSB/SPC and Fe<sub>3</sub>C@WSB/H<sub>2</sub>O<sub>2</sub> processes (reaction conditions: [DCF]<sub>0</sub> = 0.02 mM, catalyst dosage 0.1 g/L, [H<sub>2</sub>O<sub>2</sub>]<sub>0</sub> = 1.5 mM, [SPC]<sub>0</sub> = 1.0 mM, pH<sub>0</sub> = 3.2 ± 0.1).</p>
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<p>Effects of (<b>a</b>) SPC concentration, (<b>c</b>) catalyst dosage, (<b>e</b>) DCF concentration, and (<b>g</b>) coexisting anions on the degradation of DCF in Fe<sub>3</sub>C@WSB/SPC process; effects of (<b>b</b>) H<sub>2</sub>O<sub>2</sub> concentration, (<b>d</b>) catalyst dosage, (<b>f</b>) DCF concentration, and (<b>h</b>) coexisting anions on the degradation of DCF in Fe<sub>3</sub>C@WSB/H<sub>2</sub>O<sub>2</sub> process (reaction conditions: [DCF]<sub>0</sub> = 0.02 mM, catalyst dosage 0.1 g/L, [H<sub>2</sub>O<sub>2</sub>]<sub>0</sub> = 1.5 mM, [SPC]<sub>0</sub> = 1.0 mM, pH<sub>0</sub> = 3.2 ± 0.1).</p>
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<p>(<b>a</b>) Selective quenching experiments in Fe<sub>3</sub>C@WSB/SPC process; ESR signals for (<b>b</b>) •OH; (<b>c</b>) O<sub>2</sub><sup>•−</sup> and (<b>d</b>) <sup>1</sup>O<sub>2</sub> (reaction conditions: [DCF]<sub>0</sub> = 0.02 mM, catalyst dosage 0.1 g/L, [H<sub>2</sub>O<sub>2</sub>]<sub>0</sub> = 1.5 mM, [SPC]<sub>0</sub> = 1.0 mM, [DMPO]<sub>0</sub> = 50 mM, [TMP]<sub>0</sub> = 5.0 mM).</p>
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<p>(<b>a</b>) The concentration variation kinetics of PMSO and PMSO<sub>2</sub> in different processes; (<b>b</b>) the EIS spectra of Fe<sub>3</sub>C@WSB; (<b>c</b>) the LSV curves in different processes; (<b>d</b>) the I-t curve upon the addition of SPC and DCF.</p>
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<p>(<b>a</b>) The removal performance of DCF in four consecutive cycles in Fe<sub>3</sub>C@WSB/SPC process; (<b>b</b>) the XRD pattern of used Fe<sub>3</sub>C@WSB; the (<b>c</b>) C 1s and (<b>d</b>) Fe 2p XPS of used Fe<sub>3</sub>C@WSB (reaction conditions: [DCF]<sub>0</sub> = 0.02 mM, catalyst dosage 0.1 g/L, [SPC]<sub>0</sub> = 1.0 mM, pH<sub>0</sub> = 3.2 ± 0.1).</p>
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18 pages, 6919 KiB  
Article
Behavioral, Physiological, and Molecular Mechanisms Underlying the Adaptation of Helicoverpa armigera to the Fruits of a Marginal Host: Walnut (Juglans regia)
by Haiqiang Li, Xinzheng Huang, Long Yang, Haining Liu, Bing Liu and Yanhui Lu
Plants 2024, 13(19), 2761; https://doi.org/10.3390/plants13192761 - 1 Oct 2024
Viewed by 863
Abstract
In northwest China, changes in cultivation patterns and the scarcity of preferred hosts have forced Helicoverpa armigera to feed on the marginal host walnut (Juglans regia). However, the mechanisms allowing this adaptation remain poorly understood. Here, we investigated the behavioral, physiological, [...] Read more.
In northwest China, changes in cultivation patterns and the scarcity of preferred hosts have forced Helicoverpa armigera to feed on the marginal host walnut (Juglans regia). However, the mechanisms allowing this adaptation remain poorly understood. Here, we investigated the behavioral, physiological, and molecular mechanisms underlying the local adaptation of this pest to walnut fruits. The green husk and shell generally contained higher levels of phytochemicals than the kernel. Bioassays revealed that the phytochemical-rich green husk and shell were less preferred, reduced larval fitness and growth, and elevated the activity of detoxification enzymes compared to the nutrient-rich kernel, which were further supported by a larger number of upregulated detoxification genes in insects fed green husks or shells based on transcriptome sequencing. Together, these data suggest that P450 genes (LOC110371778) may be crucial to H. armigera adaptation to the phytochemicals of walnuts. Our findings provide significant insight into the adaptation of H. armigera to walnut, an alternative host of lower quality. Meanwhile, our study provides a theoretical basis for managing resistance to H. armigera larvae in walnut trees and is instrumental in developing comprehensive integrated pest management strategies for this pest in walnut orchards and other agricultural systems. Full article
(This article belongs to the Special Issue Integrated Pest Management—from Chemicals to Green Management)
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<p>Biplot of principal component analysis (PCA) demonstrating the variation in seven secondary metabolites in the green husk, shell, and kernel of walnut fruit. The sample points with different colors indicate different parts of walnut fruit—the green husk (green), shell (gray), and kernel (orange), respectively. Solid lines with arrows represent the secondary metabolites; the cosine of the angle between them and the PC axis indicates the correlation between them on the PC axes (a smaller angle indicates a higher correlation).</p>
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<p>Feeding preferences of <span class="html-italic">Helicoverpa armigera</span> on different parts of walnut fruits (green husk, shell, kernel) at 24 h. The different letters indicate significant differences analyzed by one-way ANOVA followed by Tukey’s tests, <span class="html-italic">p</span> &lt; 0.05.</p>
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<p>The survival rate (<b>A</b>), mortality rate (<b>B</b>), developmental duration from 2nd instar to 6th instar (<b>C</b>), and pupal weight (<b>D</b>) of <span class="html-italic">Helicoverpa armigera</span> fed on different parts of walnut fruits. <span class="html-italic">H. armigera</span> fed an artificial diet were used as the control (CK). The different letters indicate significant differences analyzed by one-way ANOVA followed by Tukey’s tests, <span class="html-italic">p</span> &lt; 0.05.</p>
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<p>Fresh weight (<b>A</b>), dry weight (<b>B</b>), and water content (<b>C</b>) of 5th-instar larvae of <span class="html-italic">Helicoverpa armigera</span> fed on different parts of walnut fruits at 48 h. <span class="html-italic">H. armigera</span> fed an artificial diet were used as the control (CK). The different letters indicate significant differences analyzed by one-way ANOVA followed by Tukey’s tests, <span class="html-italic">p</span> &lt; 0.05.</p>
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<p>Detoxification enzyme activities of <span class="html-italic">Helicoverpa armigera</span> fed on different parts of walnut fruits at two different time points. The enzyme activity of P450 at 24 h (<b>A</b>) and 48 h (<b>B</b>), the activity of CarE at 24 h (<b>C</b>) and 48 h (<b>D</b>), and the activity of GST at 24 h (<b>E</b>) and 48 h (<b>F</b>). <span class="html-italic">H. armigera</span> fed an artificial diet were used as the control (CK). The different letters indicate significant differences analyzed by one-way ANOVA followed by Tukey’s tests, <span class="html-italic">p</span> &lt; 0.05.</p>
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<p>Differentially expressed genes (DEGs) in <span class="html-italic">Helicoverpa armigera</span> fed on different parts of walnut fruits at two different time points. Number of up- and downregulated DEGs (<b>A</b>) and Venn diagram of common and unique DEGs (<b>B</b>) at 24 h. Number of up- and downregulated DEGs (<b>C</b>) and Venn diagram of common and unique DEGs (<b>D</b>) at 48 h.</p>
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<p>Expression profiles based on K-means with clustering of genes differentially expressed in at least one control–treatment comparison at 24 (<b>A</b>) and 48 h (<b>B</b>).</p>
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<p>Functional classification of differentially expressed genes (DEGs) in the green husk treatment at 24 h (<b>A</b>) and 48 h (<b>B</b>), in the shell treatment at 24 h (<b>C</b>) and 48 h (<b>D</b>), and in the kernel treatment at 24 h (<b>E</b>) and 48 h (<b>F</b>).</p>
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<p>P450 genes differentially expressed in at least one control–treatment comparison in RNA-seq (<b>A</b>) and selected P450 genes in qRT-PCR (<b>B</b>) at 24 h. P450 genes differentially expressed in RNA-seq (<b>C</b>) and selected P450 genes in qRT-PCR (<b>D</b>) at 48 h. Downward-pointing bars depict downregulation and upward pointing bars depict upregulation.</p>
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14 pages, 1572 KiB  
Article
The Influence of Drying Sewage Sludge with the Addition of Walnut Shells on Changes in the Parameters and Chemical Composition of the Mixture
by Sebastian Kujawiak, Małgorzata Makowska, Bogusława Waliszewska, Damian Janczak, Jakub Brózdowski, Wojciech Czekała and Artur Zyffert
Energies 2024, 17(18), 4701; https://doi.org/10.3390/en17184701 - 21 Sep 2024
Viewed by 841
Abstract
One method of preparing sludge for management and use is solar drying. To intensify the drying process, natural lignocellulosic additives can be used to alter the structure of the sludge and accelerate water evaporation. Light, hard materials with low absorption capacity are best [...] Read more.
One method of preparing sludge for management and use is solar drying. To intensify the drying process, natural lignocellulosic additives can be used to alter the structure of the sludge and accelerate water evaporation. Light, hard materials with low absorption capacity are best suited for this purpose, e.g., walnut shells, which are unused waste. The aim of the study was to determine the impact of the evaluation of walnut shells on the sludge drying process and to assess the impact of the drying process on the chemical, physical, and fuel properties of the additive. The moisture content, crushing strength, chemical composition, and physical and fuel properties of mixtures were determined. A small addition of walnut shells (25%) was found to accelerate the drying process even in winter and spring (up to 30 days) compared to sludge without additives. Walnut shells retain their chemical composition and strength despite unfavourable conditions and a chemically aggressive environment, indicating they may be reused. The mixture containing sewage sludge and walnut shells has a calorific value of 15.6 MJ/kg, which is similar to wood; it is also fully biodegradable and suitable as a fertiliser to improve soil structure, as it contains approx. 80–90% DM (including approx. 40% carbon, 3% nitrogen, and other elements, such as phosphorus and potassium.) Full article
(This article belongs to the Special Issue Environmentally Friendly Biofuel Production 2024)
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<p>Measuring automation set for a solar drying tunnel.</p>
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<p>Drying curves for the preliminary series of tests (<b>A</b>), drying curves for the basic test series (<b>B</b>).</p>
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<p>Graph showing temperature changes with respect to external factors in the basic series of tests (<b>A</b>), and graph showing humidity changes with respect to external factors during the basic series of tests (<b>B</b>).</p>
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<p>IR spectra of walnut shell mixtures.</p>
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<p>Values of gas oxides in the flue gas.</p>
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23 pages, 5146 KiB  
Article
Flame Retardancy and Thermal Stability of Rigid Polyurethane Foams Filled with Walnut Shells and Mineral Fillers
by Sylwia Makowska, Karolina Miedzińska, Agnė Kairytė, Jurga Šeputytė-Jucikė and Krzysztof Strzelec
Materials 2024, 17(18), 4629; https://doi.org/10.3390/ma17184629 - 21 Sep 2024
Viewed by 1004
Abstract
Recently, the influence of the concept of environmental sustainability has increased, which includes environmentally friendly measures related to reducing the consumption of petrochemical fuels and converting post-production feedstocks into raw materials for the synthesis of polymeric materials, the addition of which would improve [...] Read more.
Recently, the influence of the concept of environmental sustainability has increased, which includes environmentally friendly measures related to reducing the consumption of petrochemical fuels and converting post-production feedstocks into raw materials for the synthesis of polymeric materials, the addition of which would improve the performance of the final product. In this regard, the development of bio-based polyurethane foams can be carried out by, among other things, modifying polyurethane foams with vegetable or waste fillers. This paper investigates the possibility of using walnut shells (WS) and the mineral fillers vermiculite (V) and perlite (P) as a flame retardant to increase fire safety and thermal stability at higher temperatures. The effects of the fillers in amounts of 10 wt.% on selected properties of the polyurethane composites, such as rheological properties (dynamic viscosity and processing times), mechanical properties (compressive strength, flexural strength, and hardness), insulating properties (thermal conductivity), and flame retardant properties (e.g., ignition time, limiting oxygen index, and peak heat release) were investigated. It has been shown that polyurethane foams containing fillers have better performance properties compared to unmodified polyurethane foams. Full article
(This article belongs to the Special Issue Advances in Bio-Polymer and Polymer Composites)
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<p>Scheme for the synthesis of polyurethane foams.</p>
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<p>Optical image of walnut shells at magnification of (<b>a</b>) 50 and (<b>b</b>) 100.</p>
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<p>Optical images of (<b>a</b>,<b>b</b>) perlite, and (<b>c</b>,<b>d</b>) vermiculite at 50× (<b>a</b>,<b>c</b>,) and 100× (<b>b</b>,<b>d</b>,) magnification.</p>
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<p>Size distribution of fillers: (<b>a</b>) walnut shells; (<b>b</b>) vermiculite; and (<b>c</b>) perlite.</p>
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<p>FTIR spectra of (<b>a</b>) walnut shells, (<b>b</b>) perlite, and (<b>c</b>) vermiculite.</p>
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<p>Thermogravimetric and derivative thermogravimetric results of walnut shells (<b>a</b>,<b>b</b>), vermiculite, and perlite (<b>c</b>,<b>d</b>).</p>
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<p>Morphology of polyurethane foams (<b>a</b>), polyurethane foams with walnut shells (<b>b</b>), polyurethane foams with the addition of walnut shells and perlite (<b>c</b>–<b>f</b>), polyurethane foams with the addition of walnut shells and vermiculite (<b>g</b>–<b>j</b>).</p>
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<p>Effect of walnut shells and perlite (<b>a</b>) and walnut shells and vermiculite (<b>b</b>) on apparent density and hardness of polyurethane foams.</p>
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<p>Effect of walnut shells and perlite (<b>a</b>) and walnut shells and vermiculite (<b>b</b>) on compressive strength of polyurethane foams.</p>
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<p>Effect of walnut shells and perlite (<b>a</b>) and walnut shells and vermiculite (<b>b</b>) on flexural strength and elongation of polyurethane foams.</p>
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<p>Water uptake and contact angle results of polyurethane foams with the addition of walnut shells and perlite (<b>a</b>), and walnut shells and vermiculite (<b>b</b>).</p>
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<p>Thermogravimetric (TGA) and derivative thermogravimetry (DTG) results of polyurethane foams with the addition of walnut shells and perlite (<b>a</b>,<b>b</b>), and walnut shells and vermiculite (<b>c</b>,<b>d</b>).</p>
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<p>Thermal conductivity of foams with the addition of walnut shells and perlite (<b>a</b>) and walnut shells and vermiculite (<b>b</b>) at average temperatures of 10, 20, and 40 °C.</p>
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18 pages, 6444 KiB  
Article
Design and Optimization of Key Parameters for a Machine Vision-Based Walnut Shell–Kernel Separation Device
by Peng Ni, Shiqi Hu, Yabo Zhang, Wenyang Zhang, Xin Xu, Yuheng Liu, Jiale Ma, Yang Liu, Hao Niu and Haipeng Lan
Agriculture 2024, 14(9), 1632; https://doi.org/10.3390/agriculture14091632 - 18 Sep 2024
Viewed by 1080
Abstract
The separation of walnut kernels and shells has long been regarded as a bottleneck, limiting processing efficiency, product quality, and industry advancement. In response to the challenges of improving separation accuracy and the inadequacy of existing equipment for meeting industry demands, this paper [...] Read more.
The separation of walnut kernels and shells has long been regarded as a bottleneck, limiting processing efficiency, product quality, and industry advancement. In response to the challenges of improving separation accuracy and the inadequacy of existing equipment for meeting industry demands, this paper proposes an innovative walnut shell–kernel separation device based on machine vision technology. An experimental system was constructed, and key parameters were optimized to enhance its performance. The device comprises five main modules: material conveyance, image acquisition, control module, sorting module, and frame. Differential separation technology is used to convert the walnut material group into a stable particle flow, addressing the issue of missed selections due to material blockages. An enhanced YOLOv8n algorithm improves small object detection and interference resistance, enabling accurate identification of walnut kernels. The Box–Behnken Design and Artificial Neural Network prediction model was used to determine the optimal operating parameters for the device. Experimental results showed that effective differential separation was achieved when the dual-stage conveyor system operated at speeds of 0.2 m/s and 1 m/s. The improved I-YOLOv8n algorithm reached an accuracy of 98.8%. Using the neural network model, the optimal operational parameters were determined: an air pressure of 0.72 MPa, a jetting component angle of 10.16°, and a sorting height of 105.12 cm. Under these conditions, the device achieved an actual cleaning rate of 93.56%, demonstrating outstanding separation performance. Compared to traditional separation methods, this device offers significant advantages in terms of efficiency, quality, and ease of operation, providing new technological pathways and support for the automation and intelligent transformation of the walnut processing industry. In the future, the device is expected to undergo further improvements to meet broader market demand and serve as a reference for the separation of other agricultural products. Full article
(This article belongs to the Section Agricultural Technology)
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<p>A schematic diagram of the structure model of the walnut shell–kernel separation device.</p>
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<p>The acquisition process for walnut shell and kernel mixture materials.</p>
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<p>A simulation model for walnut shell and kernel materials.</p>
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<p>Material image acquisition.</p>
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<p>A diagram of the improved network model structure.</p>
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<p>A prototype of the walnut shell–kernel separation device.</p>
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<p>Sorting module structure diagram.</p>
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<p>Neural network structure.</p>
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<p>Simulation for material conveyance module.</p>
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<p>Object detection performance under occlusion conditions.</p>
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<p>The relationship between predicted and actual cleaning rates: (<b>a</b>) predicted value–actual value; (<b>b</b>) predicted value residual.</p>
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<p>Effects of air pressure, angle, and sorting height on cleaning rate: (<b>a</b>) air pressure and angle; (<b>b</b>) air pressure and sorting height; (<b>c</b>) angle and sorting height.</p>
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<p>Neural network prediction diagram.</p>
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12 pages, 1598 KiB  
Article
An Analysis of the Physicochemical and Energy Parameters of Briquettes Manufactured from Sewage Sludge Mixtures and Selected Organic Additives
by Sebastian Kujawiak, Małgorzata Makowska, Damian Janczak, Wojciech Czekała, Włodzimierz Krzesiński, Ariel Antonowicz and Karol Kupryaniuk
Energies 2024, 17(18), 4573; https://doi.org/10.3390/en17184573 - 12 Sep 2024
Viewed by 714
Abstract
As a by-product of wastewater treatment, sewage sludge can be used for natural, agricultural, or energy purposes. One method of preparing sludge for management and use is solar drying. To intensify the drying process, natural additives can be used to alter the structure [...] Read more.
As a by-product of wastewater treatment, sewage sludge can be used for natural, agricultural, or energy purposes. One method of preparing sludge for management and use is solar drying. To intensify the drying process, natural additives can be used to alter the structure of the sludge and accelerate the evaporation of water. This research aimed to evaluate the influences of different organic additives in sewage sludge mixtures on the physicochemical and energy parameters of briquettes. This research was carried out without thermal boosting in a 4 × 2.5 × 2 m plastic tunnel. The tunnel was equipped with three drying stations and control and measuring equipment. In two test series, sludge additives in the form of straw and lignocellulosic materials, sawdust, bark, woodchips, and walnut shells, were used. Briquettes were made from the resulting mixtures and then subjected to physical and chemical analyses. This research showed high variability in the contents of trace elements, nitrogen, and sulphur in relation to an increase in the amount of sludge in the briquettes, which, for the briquettes made from sewage sludge, was nearly twice as high as for the briquettes made from the mixtures. The results of the flue gas analysis for the briquettes with sawdust and wood chip additives were very similar. The briquettes made from sewage sludge with lignocellulosic materials (bark and wood chips) had fuel properties similar to woody biomass, with a calorific value and heat of combustion of 15–16 MJ/kg. Fibrous additives (straw) significantly increased the strength parameters of the briquettes, by more than 50% of the value. The compositions and properties of the mixtures affected the following briquetting parameters: temperature and compressive force. The briquettes made from sewage sludge and additives can be classified according to ISO 21640 as SRFs (solid recovered fuels). In most of the results, the net calorific value (NCV) was 3 to 4; the chlorine content (CL) was 2 to 1; and the mercury content (Hg) was 1. The sewage sludge mixtures facilitated the agricultural and energy use of the briquettes. Full article
(This article belongs to the Special Issue Biofuel Production and Bio-Waste Management)
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<p>Measuring automation set for a solar-drying tunnel (to be reproduced in colour on the web and in black-and-white in print).</p>
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<p>The process of briquetting mixes.</p>
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<p>Briquettes produced from mixtures.</p>
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<p>Contents of carbon monoxide, sulphur oxides, and nitrogen oxides in flue gases from analysed mixtures.</p>
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<p>Mechanical strengths of briquettes according to ISO 17831-2:2015.</p>
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18 pages, 8468 KiB  
Article
One-Stage Synthesis of Microporous Carbon Adsorbents from Walnut Shells—Evolution of Porosity and Structure
by Ilya E. Men’shchikov, Andrey A. Shiryaev, Andrey V. Shkolin, Alexander E. Grinchenko, Elena V. Khozina, Alexey A. Averin and Anatolii A. Fomkin
C 2024, 10(3), 79; https://doi.org/10.3390/c10030079 - 2 Sep 2024
Viewed by 854
Abstract
One-stage synthesis technology for preparing carbon adsorbents with tailored porosity from agricultural waste is worthwhile due to their extensive application value. Thermal gravimetric analysis, low-temperature N2 adsorption, X-ray diffraction (XRD), small-angle X-ray scattering (SAXS), and Raman spectroscopy were used to record the [...] Read more.
One-stage synthesis technology for preparing carbon adsorbents with tailored porosity from agricultural waste is worthwhile due to their extensive application value. Thermal gravimetric analysis, low-temperature N2 adsorption, X-ray diffraction (XRD), small-angle X-ray scattering (SAXS), and Raman spectroscopy were used to record the structure transformations of carbon materials, namely pore development, proceeding in the course of the step-wise pyrolysis of renewable and low-cost raw materials such as walnut shells (WNSs), which was carried out within a temperature range of 240–950 °C in a CO2 flow. The minimum threshold carbonization temperature for preparing nanoporous carbon materials from WNSs, determined by the examination of the N2 adsorption data, was 500 °C. The maximum specific micropore volume and BET surface achieved in the process without holding a material at a specified temperature were only 0.19 cm3/g and 440 m2/g, respectively. The pyrolysis at 400–600 °C produced amorphous sp2 carbon. At a temperature as high as 750 °C, an increase in the X-ray reflection intensity indicated the ordering of graphite-like crystallites. At high burn-off degrees, the size of coherently scattering domains becomes smaller, and an increased background in X-ray patterns indicates the destruction of cellulose nanofibrils, the disordering of graphene stacks, and an increase in the amount of disordered carbon. At this stage, pores develop in the crystallites. They are tentatively assigned to crystallites with sizes of 15–20 nm and to micropores. According to the Raman spectra combined with the XRD and SAXS data, the structure of all the pyrolysis products is influenced by the complex structure of the walnut shell precursor, which comprises cellulose nanofibrils embedded in lignin. This structure was preserved in the initial stage of pyrolysis, and the graphitization of cellulose fibrils and lignin proceeds at different rates. Most of the pores accessible for gas molecules in the resulting carbon materials are associated with former cellulose fibrils. Full article
(This article belongs to the Special Issue Characterization of Disorder in Carbons (2nd Edition))
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<p>Diagram of obtaining carbon adsorbents of CW and AW series in temperature conditions of processing WNS particles. The transition of the color of the symbols representing CW1–CW7 samples from violet to orange indicates an increase in pyrolysis temperature, and the color changes from orange to black in the AW series show an increase in degree of burn-off. The dark green symbol shows the CW8 sample, which was not further activated.</p>
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<p>Weight losses in the CW materials during the carbonization process (<b>a</b>) plotted as a function of the carbonization temperature (top axis) and duration of the entire synthesis (bottom axis), and weight losses in the AW materials during the activation (<b>b</b>) plotted versus the duration of the total synthesis (bottom axis) and the activation (top axis) processes. The vertical dashed lines in (<b>a</b>) indicate the regions corresponding to the stages in the formation of carbonizate (I), (II), and (III); the vertical lines in (<b>b</b>) show the evolution of carbonizate into activated carbons. Weight(s) is the mass of a sample with respect to the initial mass of the precursor (WNS); weight (C) is the mass of a sample with respect to the initial mass of the carbonizate prepared at 900 °C. The evolution in the color corresponds to an increase in the pyrolysis temperature (<b>a</b>) and burn-off degree (<b>b</b>) in accordance with <a href="#carbon-10-00079-f001" class="html-fig">Figure 1</a>.</p>
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<p>(<b>a</b>) The <span class="html-italic">N</span><sub>2</sub> adsorption (solid symbols)/desorption (open symbols) isotherms at 77 K for the carbon materials CW4 (1), CW5 (2), CW6 (3), CW7 (4), and CW8 (5) prepared from the WNS precursor by pyrolysis at temperature <span class="html-italic">T</span><sub>C</sub>, °C: 500, 600, 750, 900, and 950. (<b>b</b>) The <span class="html-italic">N</span><sub>2</sub> adsorption (solid symbols)/desorption (open symbols) isotherms at 77 K for the carbon materials of the AW series, AW1/CW7 (1), AW2 (2), AW3 (3), AW4 (4), AW5 (5), and AW6 (6), with different burn-off degrees, %: 0, 10, 20, 30, 45, and 70. Symbols show the experimental data, and lines are the approximations.</p>
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<p>Pore size distribution calculated by the QSDFT method based on the low-temperature nitrogen vapor adsorption in AW series carbon materials: AW1 (1), AW3 (2), AW5 (3), and AW6 (4).</p>
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<p>XRD patterns recorded for the carbon materials of the CW (<b>a</b>) and AW (<b>b</b>) series.</p>
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<p>Small-angle X-ray scattering from carbonizates of CW series prepared at different carbonization temperatures (<b>a</b>) and activated carbon materials of AW series with different burn-off degrees (<b>b</b>).</p>
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<p>Small-angle X-ray scattering from carbonizates of CW series prepared at different carbonization temperatures (<b>a</b>) and activated carbon materials of AW series with different burn-off degrees (<b>b</b>).</p>
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<p>The first- and second-order Raman spectra for the CW (<b>a</b>) and AW (<b>b</b>) carbon materials, and the decomposition of the first-order spectrum for AW4 into five components shown as an example (<b>c</b>). The curves are vertically shifted for clarity. The excitation wavelength is shown on the right.</p>
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<p>The dependence of the positions of the G- (solid symbols, left and bottom axes) and A-peaks (right and top axes, open symbols) on their FWHM parameters at the excitation wavelength of 532 nm (green symbols) and 785 nm (red symbols) for CW3–CW8 and AW1/CW7–AW6.</p>
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<p>The ratio of intensities of the D- and G-peaks, <span class="html-italic">I</span>(D)/<span class="html-italic">I</span>(G) (bottom), and their analogs, <span class="html-italic">I</span>(D<sub>broad</sub>)/<span class="html-italic">I</span>(A) (top), versus specific BET surfaces, which depend on the burn-off degree. The dashed lines indicate the trend of the changes in the intensity ratios with an increase in the burn-off degree.</p>
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<p>The ratio of the intensities of the A- and G-peaks, <span class="html-italic">I</span>(A)/<span class="html-italic">I</span>(G), versus the characteristic energy of adsorption (<b>a</b>) and specific BET surface (<b>b</b>). The lines indicate the qualitative correlation trends with an increase in the burn-off degree.</p>
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14 pages, 5907 KiB  
Article
Biochar Catalysis for the Enhanced Abiotic Humification of Polyphenols: An Important Mechanism Helping Sequester Carbon
by Jiangmin Zhou, Ziru Zhou, Chuanqing Yao, Yujie Zhang, Han Ren, Guining Lu and Hualin Chen
Agronomy 2024, 14(9), 1951; https://doi.org/10.3390/agronomy14091951 - 29 Aug 2024
Viewed by 669
Abstract
Abiotic humification, dominated by catalytic oxidation, is one of the critical mechanisms for organic carbon preservation in nature. However, the effects of biochar catalysis on abiotic humification have not yet been elucidated. This study investigated the catalytic power of biochar from walnut shells [...] Read more.
Abiotic humification, dominated by catalytic oxidation, is one of the critical mechanisms for organic carbon preservation in nature. However, the effects of biochar catalysis on abiotic humification have not yet been elucidated. This study investigated the catalytic power of biochar from walnut shells at different temperatures (300 °C, 600 °C, and 900 °C) for the abiotic transformation of hydroquinone (HQ) as a representative polyphenol. All the biochar samples catalyzed HQ polymerization, resulting in the formation of humic polymers such as fulvic acids (FAs) and humic acids (HAs). Light and oxygen promoted HA formation. HO was detected in the BC600–HQ reaction system, and HO quenching resulted in a 41.22% decrease in HA production, indicating that HO plays a major role in the oxidative polymerization. In the proposed pathway for the abiotic humification, biochar active sites and generated reactive oxygen species accept an electron from HQ, resulting in oxidation to (semi)quinone radicals, which subsequently undergo cleavage or a coupling reaction to form the oligomerized products. Under BC600 catalysis, the weight-average molecular weight (Mw) of the reaction products of HQ, glucose, and glycine reached 14,449 Da. These findings provide new insights into the application potential of biochar for promoting soil carbon sequestration. Full article
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Figure 1

Figure 1
<p>Changes in BC600–HQ system during the 360 h reaction under dark and oxygen-poor conditions. ((<b>A</b>) HQ concentration, (<b>B</b>) DOC concentration, (<b>C</b>) UV–Vis absorbance value at 400 nm, (<b>D</b>) ratio of UV–Vis absorbance value at 400 nm and 600 nm, (<b>E</b>) pH value, (<b>F</b>) FA and HA concentration).</p>
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<p>Impact of light and oxygen on abiotic humification during the 360 h reaction. ((<b>A</b>) DOC concentration. (<b>B</b>) pH value. (<b>C</b>) FA concentration. (<b>D</b>) HA concentration).</p>
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<p>HO<sup>•</sup> detection with DMPO as the spin-trapping agent and HO<sup>•</sup> quenching experiment in the BC600–HQ system during the 360 h reaction. ((<b>A</b>) EPR spectra of DMPO-HO<sup>•</sup> adduct, (<b>B</b>) DOC concentration, (<b>C</b>) pH value, (<b>D</b>) FA concentration, (<b>E</b>) HA concentration).</p>
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<p>(<b>A</b>) Comparison of HA concentration catalyzed by biochar prepared at 300 °C (BC300), 600 °C (BC600), and 900 °C (BC900). (<b>B</b>) Persistent free radicals (PFRs) of BC300, BC600, and BC900 before reaction. (<b>C</b>) Raman spectra of BC300, BC600, and BC900. (<b>D</b>) PFRs of BC300, BC600, and BC900 after reaction.</p>
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<p>Total ion chromatogram (TIC) of GC–MS for (<b>A</b>) BC600–HQ reaction system and (<b>B</b>) control system (only BC600).</p>
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<p>Graphical scheme for proposed route of HQ abiotic humification reaction under BC600 catalysis.</p>
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