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Search Results (4,217)

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Keywords = carbon dioxide (CO2)

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15 pages, 2713 KiB  
Article
A Strategy for the Production of Single-Cell Proteins by the Efficient and Continuous Fermentation of Hydroxide Bacteria Under Gas Fermentation
by Shuai Fu, Longyu Gou, Ke Long, Lanchai Chen, Dingrong Cai and Yue Lu
Appl. Sci. 2025, 15(2), 540; https://doi.org/10.3390/app15020540 - 8 Jan 2025
Abstract
Cupriavidus necator can produce single-cell proteins (SCPs) using electrons produced by hydrogen as energy, oxygen as electron acceptors, and CO2 as carbon sources. Gas fermentation is a process of microbial fermentation that uses gas substrates (such as hydrogen, carbon dioxide, etc.) which [...] Read more.
Cupriavidus necator can produce single-cell proteins (SCPs) using electrons produced by hydrogen as energy, oxygen as electron acceptors, and CO2 as carbon sources. Gas fermentation is a process of microbial fermentation that uses gas substrates (such as hydrogen, carbon dioxide, etc.) which faces several challenges, mainly including the low solubility of gas substrates, the danger of hydrogen and oxygen mixing, and the optimization of fermentation conditions. To overcome these challenges, this article explores a variety of strategies—including the design of a self-developed bioreactor—to reduce the risk of static electricity. Without the addition of filler material, the results showed that the maximum cell dry weight (CDW) of 30% secondary seed inoculation was 20.41% higher than that of 10% secondary seed inoculum, and 5.99% higher than that of 20% secondary seed inoculum. Combined with the filler material and with the use of high-efficiency continuous fermentation technology, the average yield of continuous fermentation was 23.31 g/day, while the average yield of batch fermentation was 14.33 g/day. The daily yield of continuous fermentation is 1.63 times that of batch fermentation. These efforts are aimed at improving the efficiency and safety of gas fermentation. Full article
(This article belongs to the Topic Sustainable Food Production and High-Quality Food Supply)
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<p>CO<sub>2</sub> fixation flow chart of microbial fermentation for SCP production.</p>
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<p>Diagram of the installation of high-efficiency continuous fermentation equipment.</p>
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<p>Fermentation, in batches containing inoculation amounts of 10% (■), 20% (●), and 30% (▲), for 144 h in a 5 L reactor at atmospheric pressure. Optical density was measured at 620 nm (<b>a</b>) and the cell dry weight was also measured (<b>b</b>). The effect of the inoculum amount on fermentation under conditions of optimal filling was assessed. The filling material was stainless steel with a filling volume of 500 cm<sup>3</sup> on the top and 500 cm<sup>3</sup> on the bottom (<b>c</b>). All mean values were taken from three samples.</p>
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<p>Stainless steel (<b>A</b>) and plastic (<b>B</b>) fillers. The stainless steel has a saddling shape, and the shape of the plastic is cylindrical; both materials’ shapes are 9 mm long and 5 mm wide.</p>
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<p>The effect of stainless steel and plastic materials on fermentation (<b>a</b>). The effect of different filling amounts on fermentation (<b>b</b>). The filling material is located in the gas exchange unit in the upper part of the self-developed bioreactor, and the gas exchange device is divided into upper and lower parts. A: 0 cm<sup>3</sup> on the top and 0 cm<sup>3</sup> on the bottom; B: 250 cm<sup>3</sup> on the top and 250 cm<sup>3</sup> on the bottom; C: 500 cm<sup>3</sup> on the top and 500 cm<sup>3</sup> on the bottom; D: 1000 cm<sup>3</sup> on the top and 1000 cm<sup>3</sup> on the bottom.</p>
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<p>Log (colony count/mL) (<b>a</b>) and CDW (<b>b</b>) of efficient continuous fermentation by <span class="html-italic">C. necator</span> in a self-developed 5 L bioreactor at atmospheric pressure. The CDW value of the fermentation broth was harvested from five batches of continuous fermentation (<b>c</b>). When the fermentation entered its equilibrium phase, the fermentation broth and the supplementary culture broth were set, at the same time, at a rate of 0.7675 mL/min.</p>
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17 pages, 5421 KiB  
Article
Supercritical CO2-Stable Cementing Materials Based on Vinyl Ester Resin for Maintaining Wellbore Integrity
by Zhong Li, Zhiming Yin, Dingzhao Zhou, Zhiqiang Wu, Daohang Wang, Shuwen Guan and Guangyan Du
Materials 2025, 18(2), 244; https://doi.org/10.3390/ma18020244 - 8 Jan 2025
Abstract
Ensuring long-term wellbore integrity is critical for carbon dioxide geological storage. Ordinary Portland cement (PC) is usually used for wellbore primary cementing and plug operation, and set cement is easily corroded by acidic fluids, such as carbon dioxide, in underground high-temperature and high-pressure [...] Read more.
Ensuring long-term wellbore integrity is critical for carbon dioxide geological storage. Ordinary Portland cement (PC) is usually used for wellbore primary cementing and plug operation, and set cement is easily corroded by acidic fluids, such as carbon dioxide, in underground high-temperature and high-pressure (HTHP) environments, resulting in a decrease in the mechanical properties and an increase in permeability. In order to achieve long-term wellbore integrity in a CO2-rich environment This study introduces materials such as thermosetting vinyl ester resin (TSR), filler composite resin (FCR), and low-cost resin cement (RC). Corrosion experiments were conducted using four materials in 28 days under supercritical carbon dioxide gas and water phase conditions of 60 °C and 10 MPa. The samples were characterized through mechanical property testing machines, core permeability measuring instruments, FTIR, XRD, and SEM. The results proved that after corrosion, PC mechanical properties decreased, the permeability increased, and the microscopic composition and morphology changed greatly. Penetrating corrosion occurs in the sample in the gas phase environment, and propulsive corrosion from outside to inside occurs in the water phase environment. However, TSR, FCR, and RC materials all maintain excellent resistance to carbon dioxide corrosion in gas and water environments. They have higher compressive strength and extremely low permeability compared to ordinary Portland cement. These three materials’ compressive strengths can be maintained around 131, 99, and 58 MPa, and permeability can be stabilized at <6 × 10−7, <6 × 10−7, and 0.16 mD levels. In summary, the above three materials all show better performance than ordinary Portland cement and are promising alternative materials that can be used in primary cementing and plug operations of carbon dioxide geological storage wells. Full article
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<p>Schematic diagram of possible leakage paths in abandoned wells: (<b>a</b>) between casing and cement stone; (<b>b</b>) between cement plug and casing; (<b>c</b>) through cement stone pore space due to cement stone degradation; (<b>d</b>) through casing due to corrosion pipe; (<b>e</b>) through cracks in cement stone; (<b>f</b>) cracks between cement stone and rock [<a href="#B18-materials-18-00244" class="html-bibr">18</a>].</p>
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<p>Schematic diagram of static corrosion device of the high-temperature and high-pressure (HTHP) reactor.</p>
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<p>Variation of plugging agent viscosity with temperature for different SEBS contents.</p>
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<p>Consistency variation diagram during TSR curing.</p>
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<p>TG and DTG diagram of the TSR-cured body.</p>
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<p>Changes in the compressive strength of materials before and after corrosion in gas phase and water phase environments.</p>
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<p>FTIR spectrum at different depths of TSR samples after 28 days of gas phase and water phase corrosion.</p>
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<p>FTIR spectrum at different depths of FCR samples after 28 days of gas phase and water phase corrosion.</p>
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<p>XRD spectrum at different depths of PC samples after 28 days of gas phase and water phase corrosion.</p>
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<p>XRD spectrum at different depths of RC samples after 28 days of gas phase and water phase corrosion.</p>
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<p>SEM images of four types of core samples without corrosion: (<b>a</b>) Thermosetting vinyl ester resin (TSR); (<b>b</b>) Filler composite resin (FCR); (<b>c</b>) Resin cement (RC); (<b>d</b>) Polland Cement (PC).</p>
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<p>SEM images of cross-sections at different corrosion depths after 28 days of gas phase and water phase corrosion of core samples of four materials.</p>
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15 pages, 12625 KiB  
Article
Exploring the Thermodynamics and Dynamics of CO2 Using Rigid Models
by Lucas Avila Pinheiro, Walas Silva-Oliveira, Elizane E. de Moraes and José Rafael Bordin
Processes 2025, 13(1), 148; https://doi.org/10.3390/pr13010148 - 8 Jan 2025
Viewed by 194
Abstract
Understanding the behavior of carbon dioxide (CO2) under varying thermodynamic conditions is essential for optimizing processes such as Carbon Capture and Storage (CCS) and supercritical fluid extraction. This study employs molecular dynamics (MD) simulations with the EPM2 and TraPPE-small force fields [...] Read more.
Understanding the behavior of carbon dioxide (CO2) under varying thermodynamic conditions is essential for optimizing processes such as Carbon Capture and Storage (CCS) and supercritical fluid extraction. This study employs molecular dynamics (MD) simulations with the EPM2 and TraPPE-small force fields to examine CO2 phase behavior, structural characteristics, and transport properties across a temperature range of 228–500 K and pressures from 1 to 150 atm. Our findings indicate a good agreement between simulated and experimental liquid–vapor coexistence curves, validating the capability of both force fields to model CO2 accurately in a wide range of thermodynamical conditions. Radial distribution functions (RDFs) reveal distinct interaction patterns in liquid and supercritical phases, while mean squared displacement (MSD) analyses show diffusivity increasing from 5.2×109 m2/s at 300 K to 1.8×108 m2/s at 500 K. Additionally, response functions such as the heat capacity effectively capture phase transitions. These findings provide quantitative insights into CO2 phase behavior and transport properties, enhancing the predictive reliability of simulations for CCS and related industrial technologies. This work bridges gaps in the CO2 modeling literature and highlights the potential of MD simulations in advancing sustainable applications. Full article
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<p>Temperature vs. density (<span class="html-italic">T</span> vs. <math display="inline"><semantics> <mi>ρ</mi> </semantics></math>) isobars for CO<sub>2</sub> using the TraPPE-small (<b>a</b>) and EPM2 (<b>b</b>) models. The densities were estimated as the mean value along the simulations. Error bars are smaller than the points. The red dashed line represents the experimental coexistence line at saturation pressure, obtained from Ref. [<a href="#B29-processes-13-00148" class="html-bibr">29</a>]. The simulations cover a pressure range of 1–150 atm, while the experimental coexistence line corresponds to equilibrium data under vapor–liquid conditions.</p>
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<p><span class="html-italic">P</span> vs. <math display="inline"><semantics> <mi>ρ</mi> </semantics></math> diagrams for CO<sub>2</sub> using the TraPPE-small (<b>a</b>) and EPM2 (<b>b</b>) models. The simulations were performed over a temperature range of 228–500 K. Experimental points obtained from Ref. [<a href="#B49-processes-13-00148" class="html-bibr">49</a>] correspond to isothermal measurements near the CO<sub>2</sub> critical region.</p>
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<p>Specific heat capacity (<math display="inline"><semantics> <msub> <mi>C</mi> <mi>p</mi> </msub> </semantics></math>) as a function of temperature and pressure for CO<sub>2</sub> using two different models: TraPPE-small (<b>a</b>) and EPM2 (<b>b</b>).</p>
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<p>Mean squared displacement (MSD) for CO<sub>2</sub> at different pressures using the TraPPE force field.</p>
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<p>Mean squared displacement (MSD) for CO<sub>2</sub> at different pressures using the EPM2 force field.</p>
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<p>Diffusion coefficient (<b>a</b>) and viscosity (<b>b</b>) as a function of pressure for subcritical, critical, and supercritical temperatures. Experimental points obtained from Ref. [<a href="#B52-processes-13-00148" class="html-bibr">52</a>].</p>
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14 pages, 3248 KiB  
Article
Molecular Dynamics Simulation of CO2-ECBM Under Different Moisture Contents
by Xiaoyu Cheng, Xuanping Gong, Cheng Cheng, Quangui Li and Ziqiang Li
Energies 2025, 18(2), 239; https://doi.org/10.3390/en18020239 - 7 Jan 2025
Viewed by 384
Abstract
The interactions among water molecules, coal beds, and gases during the process of coal bed methane mining are highly complex. The water and methane (CH4)/carbon dioxide (CO2) molecules compete for adsorption and undergo a series of reactions that affect [...] Read more.
The interactions among water molecules, coal beds, and gases during the process of coal bed methane mining are highly complex. The water and methane (CH4)/carbon dioxide (CO2) molecules compete for adsorption and undergo a series of reactions that affect gas diffusion. In this study, Monte Carlo and molecular dynamics methods were used to investigate the microscopic mechanism of CH4/CO2 competitive adsorption and diffusion during CO2-enhanced coal bed methane mining (ECBM) under different moisture contents, and the geological storage potential of CO2 was predicted. The results showed that when the CO2 and water binding sites were independent of each other, the water molecules changed the electrostatic potential around the coal molecules, resulting in enhanced CO2 adsorption performance, as verified by the surface electrostatic potential. When the water molecules formed a water molecule layer, the adsorption capacity of the secondary adsorption sites provided was larger than that of the surface of the coal molecules, so the CO2 molecules were preferentially adsorbed on the secondary adsorption sites. However, the number of secondary adsorption sites available was not as large as that on the surface of the coal molecules. The interaction energies revealed that when the displacement effect of CH4 in the process of CO2-ECBM and the sequestration effect of CO2 were considered comprehensively, the best CO2 sequestration effect and a good CH4 displacement effect were obtained at a 3% moisture content. The worst CO2 sequestration effect was found at a 5% moisture content. After CO2 injection, the main adsorption layer of CH4 shifted from X = 5 and X = 9 to X = 8.7 and X = 12.5, respectively, and obvious detachment and diffusion occurred. The distribution of the molecular motion and diffusion coefficient revealed the considerable displacement and dispersion of the gas molecules. The distribution of the gas molecular velocity and diffusion coefficient indicated that a 3% moisture content was the ideal condition for CO2 displacement of CH4, and the CO2 sequestration effect was good. Full article
(This article belongs to the Section B: Energy and Environment)
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<p>Macromolecular planar modeling.</p>
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<p>Molecular modeling of coals with different moisture contents.</p>
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<p>Flow chart of the gas injection displacement simulation.</p>
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<p>CH<sub>4</sub>/CO<sub>2</sub> adsorption and heat of adsorption curves at different moisture contents.</p>
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<p>Electrostatic potential of the CO<sub>2</sub>/water–COAL surface.</p>
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<p>Schematic of water molecule layer adsorption in coals at different moisture contents.</p>
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<p>Interaction energy curves of gas and coal molecules.</p>
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<p>Radial distribution function of CH<sub>4</sub>/CO<sub>2</sub>-COAL for the displacement process.</p>
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<p>Velocity distribution curve.</p>
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<p>MSD and diffusion coefficient curves of the coal model at different moisture contents.</p>
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34 pages, 7806 KiB  
Article
Using OCO-2 Observations to Constrain Regional CO2 Fluxes Estimated with the Vegetation, Photosynthesis and Respiration Model
by Igor B. Konovalov, Nikolai A. Golovushkin and Evgeny A. Mareev
Remote Sens. 2025, 17(2), 177; https://doi.org/10.3390/rs17020177 - 7 Jan 2025
Viewed by 224
Abstract
A good quantitative knowledge of regional sources and sinks of atmospheric carbon dioxide (CO2) is essential for understanding the global carbon cycle. It is also a key prerequisite for elaborating cost-effective national strategies to achieve the goals of the Paris Agreement. [...] Read more.
A good quantitative knowledge of regional sources and sinks of atmospheric carbon dioxide (CO2) is essential for understanding the global carbon cycle. It is also a key prerequisite for elaborating cost-effective national strategies to achieve the goals of the Paris Agreement. However, available estimates of CO2 fluxes for many regions of the world remain uncertain, despite significant recent progress in the remote sensing of terrestrial vegetation and atmospheric CO2. In this study, we investigate the feasibility of inferring reliable regional estimates of the net ecosystem exchange (NEE) using column-averaged dry-air mole fractions of CO2 (XCO2) retrieved from Orbiting Carbon Observatory-2 (OCO-2) observations as constraints on parameters of the widely used Vegetation Photosynthesis and Respiration model (VPRM), which predicts ecosystem fluxes based on vegetation indices derived from multispectral satellite imagery. We developed a regional-scale inverse modeling system that applies a Bayesian variational optimization algorithm to optimize parameters of VPRM coupled to the CHIMERE chemistry transport model and which involves a preliminary transformation of the input XCO2 data that reduces the impact of the CHIMERE boundary conditions on inversion results. We investigated the potential of our inversion system by applying it to a European region (that includes, in particular, the EU countries and the UK) for the warm season (May–September) of 2021. The inversion of the OCO-2 observations resulted in a major (more than threefold) reduction of the prior uncertainty in the regional NEE estimate. The posterior NEE estimate agrees with independent estimates provided by the CarbonTracker Europe High-Resolution (CTE-HR) system and the ensemble of the v10 OCO-2 model intercomparison (MIP) global inversions. We also found that the inversion improves the agreement of our simulations of XCO2 with retrievals from the Total Carbon Column Observing Network (TCCON). Our sensitivity test experiments using synthetic XCO2 data indicate that the posterior NEE estimate would remain reliable even if the actual regional CO2 fluxes drastically differed from their prior values. Furthermore, the posterior NEE estimate is found to be robust to strong biases and random uncertainties in the CHIMERE boundary conditions. Overall, this study suggests that our approach offers a reliable and relatively simple way to derive robust estimates of CO2 ecosystem fluxes from satellite XCO2 observations while enhancing the applicability of VPRM in regions where eddy covariance measurements of CO2 fluxes are scarce. Full article
(This article belongs to the Section Atmospheric Remote Sensing)
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Graphical abstract
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<p>Spatial distribution of OCO-2 XCO<sub>2</sub> retrievals (ppm) averaged for the study period (1 May–30 September 2021) in the EUROCOM region. The data are shown on a 0.5° × 0.5° resolution grid used in this study.</p>
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<p>Examples of spatial distributions of monthly mean values of EVI and LSWI on the EUROCOM grid: (<b>a</b>,<b>b</b>) EVI and (<b>c</b>,<b>d</b>) LSWI for the 1st (“evergreen forests”) and 6th (“cropland”) land cover classes, respectively, in July 2021. Note that grid cells in which the fraction of a given land cover type is less than 10% are left blank.</p>
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<p>(<b>a</b>,<b>b</b>) Estimates of the residence time, τ<span class="html-italic"><sub>r</sub></span>, of the remotely sensed air masses (in hours) in the study region for 5 June and 2 July 2021, respectively, for grid cells for which OCO-2 XCO<sub>2</sub> data were available on these days, along with examples of backward trajectories (see purple and brown curves with symbols; the distance between each two neighboring symbols correspond to air transport during one hour). (<b>c</b>,<b>d</b>) Attribution of the available data points for the same respective days to the two groups corresponding to smaller (1st group) and bigger (2nd group) values of τ<span class="html-italic"><sub>r</sub></span>. Note that the data points marked as “other” correspond to OCO-2 observations over water; these points were excluded from the following analysis.</p>
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<p>Schematic overview of the regional inversion system developed in this study.</p>
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<p>(<b>a</b>) Estimates of the mean NEE in May–September 2021 and (<b>b</b>) estimates of the NEE for individual months in the same period according to our calculations using VPRM-XCO<sub>2</sub> with a priori and a posteriori parameter values in comparison with corresponding estimates based on the CTE-HR, VPRM-BGC, and v10 OCO-2 MIP data. The OCO-2 MIP estimates represent the ensemble mean values of the fluxes for the LNLGIS MIP experiment. The error bars represent the 68.3 percentile confidence intervals for the prior and posterior NEE estimates obtained in this study and the spread (maximum and minimum values) of the corresponding NEE estimates derived from the results of each inversion of the MIP ensemble (see <a href="#app1-remotesensing-17-00177" class="html-app">Table S3</a>). The uncertainties in the CTE-HR and VPRM-BGC estimates were not reported.</p>
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<p>(<b>a</b>) Time series of daily GEE and TER values delivered by VPRM-XCO<sub>2</sub> before and after assimilation of OCO-2 observations and (<b>b</b>) the mean diurnal cycles of NEE according to VPRM-XCO<sub>2</sub>, VPRM-BGC, and CTE-HR. All values are integrated or averaged over the EUROCOM region. The shaded envelopes represent the 68.3 percentile confidence intervals calculated using estimates of the corresponding CO<sub>2</sub> fluxes (i.e., GEE, TER, or NEE) from the Monte Carlo experiments (see <a href="#sec2dot2dot4-remotesensing-17-00177" class="html-sec">Section 2.2.4</a>).</p>
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<p>Spatial distributions of NEE (μmol m<sup>−2</sup> s<sup>−1</sup>) as calculated (<b>a</b>,<b>b</b>) with VPRM-XCO<sub>2</sub> using with the a priori and a posteriori parameter values, respectively, and derived from the (<b>c</b>) VPRM-BGC and (<b>d</b>) CTE-HR data. The NEE values shown are averages over the entire study period.</p>
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<p>Spatial distributions of XCO<sub>2</sub> according to the CHIMERE simulations using the (<b>a</b>) prior and (<b>b</b>) posterior CO<sub>2</sub> fluxes. The simulated XCO<sub>2</sub> values were averaged over the study period and debiased (relative to the corresponding values retrieved from OCO-2 observations). The biases in the simulated XCO<sub>2</sub> fields based on the prior and posterior fluxes are estimated to be 0.25 ppm and 1.06 ppm, respectively.</p>
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<p>(<b>a</b>,<b>c</b>) Relationships between daily values of the XCO<sub>2</sub> differences defined by Equations (6) and (7) for the simulations (<span class="html-italic">y<sub>m</sub></span>) and OCO-2 observations (<span class="html-italic">y<sub>o</sub></span>), along with (<b>b</b>,<b>d</b>) dependences of the same XCO<sub>2</sub> differences on the regional residence time, τ<sub>r</sub>. Panels (<b>a</b>,<b>b</b>) show data for the entire study period, while panels (<b>c</b>,<b>d</b>) include only data from the validation subset.</p>
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<p>Values of RMSE for the monthly sets of XCO<sub>2</sub> values from the simulations and eight TCCON sites situated in the study region.</p>
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<p>(<b>a</b>) Estimates of the mean NEE and (<b>b</b>,<b>c</b>) two of the VPRM parameters that are obtained in the three sensitivity test experiments (TC1-TC3) involving synthetic XCO<sub>2</sub> data. Note that the confidence intervals in panel (<b>b</b>) are shown in terms of the 90 percentile, instead of the 68.3 percentile as in the other panels.</p>
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<p>Posterior estimates of the mean monthly NEE inferred from the OCO-2 observations using different assumptions (see <a href="#remotesensing-17-00177-t005" class="html-table">Table 5</a>) for boundary conditions of the transport model.</p>
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18 pages, 4414 KiB  
Article
Discussions on the Adsorption Behaviors Affected by the Differences Between Graphene Oxide and Graphene Grafted by Chitosan
by Chin-Chun Chung, Hua-Wei Chen, Jin-Lin Han and Hung-Ta Wu
Polysaccharides 2025, 6(1), 3; https://doi.org/10.3390/polysaccharides6010003 - 5 Jan 2025
Viewed by 627
Abstract
There are limited studies in the literature on the surface characterization of modified graphene and graphene oxide and the impact of these modified adsorbents on adsorption performance. In addition, the amine group essentially has a promising affinity for carbon dioxide (CO2). [...] Read more.
There are limited studies in the literature on the surface characterization of modified graphene and graphene oxide and the impact of these modified adsorbents on adsorption performance. In addition, the amine group essentially has a promising affinity for carbon dioxide (CO2). Therefore, chitosan was used in this study to be grafted onto graphene and graphene oxide respectively. This study examines the effects of graphene, graphene oxide, and chitosan-modified graphene oxide thin films on the removal of carbon dioxide (CO2). Thin films of graphene, graphene oxide, and their chitosan-modified counterparts were prepared via the methods of precipitation and grafting. The differences in the chemical structure, surface properties, and surface morphology of the films were evaluated, and their effect on the adsorption performance of CO2 is discussed herein. The micrographs from a scanning electron microscope (SEM) show that the surface of graphene oxide appeared to be more porous than graphene, and the amount of grafted chitosan on graphene oxide is higher than that on graphene. An analysis of atomic force microscope (AFM) finds that the surface of chitosan-modified graphene oxide is rougher than that of chitosan-modified graphene. The results of energy-dispersive X-ray spectroscopy (EDS) spectra reveal that the composition of oxygen in graphene oxide is greater than that in graphene and confirm that the oxygen and nitrogen contents of chitosan-modified adsorbents are greater than those of the pristine materials. An analysis of Fourier-transform infrared spectroscopy (FTIR) shows that most of the oxygen-containing groups are reacted or covered by amide or amine groups due to modification with chitosan. The adsorption isotherms for CO2 adsorbed by the prepared graphene and graphene oxide presented as type I, indicating great adsorption performance under low pressure. The appropriate amount of chitosan for modifying graphene oxide could be found based on the change in surface area. Although the breakthrough times and the thicknesses of the mass transfer regions for graphene oxide modified with 0.9% and 1.2% chitosan were similar, the modification of graphene oxide with 0.9% chitosan was appropriate in this study due to a significant decrease in surface area with 1.2% chitosan dosage. The adsorption uptake difference between chitosan-modified graphene oxide and graphene was greater than that without modification with chitosan due to more chitosan grafted on graphene oxide. The Toth adsorption isotherm model was used to fit the adsorption uptake, and the average deviation was about 1.36%. Full article
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<p>Microbalance adsorption system.</p>
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<p>Fixed-bed thin film adsorption system.</p>
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<p>Adsorption isotherms for different percent of chitosan added.</p>
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<p>Comparison of CO<sub>2</sub> adsorption isotherms of chitosan-modified graphene oxide in this study with those of the literature data. (●: this study; ☐: Cavenati et al., 2004; △: Giraldo et al., 2020; ○: Keramati et al., 2014; *: Hsan et al., 2020).</p>
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<p>SEM images of (<b>a</b>) graphene, (<b>b</b>) graphene oxide, (<b>c</b>) modification of graphene by chitosan, and (<b>d</b>) modification of graphene oxide by chitosan.</p>
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<p>AFM analyses for thin film of (<b>a</b>) graphene, (<b>b</b>) graphene oxide, (<b>c</b>) modification of graphene by chitosan, and (<b>d</b>) modification of graphene oxide by chitosan.</p>
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<p>Elemental composition analysis of (<b>a</b>) graphene, (<b>b</b>) graphene oxide, (<b>c</b>) modification of graphene by chitosan, and (<b>d</b>) modification of graphene oxide by chitosan.</p>
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<p>FTIR spectra (<b>a</b>) of graphene and graphene oxide; (<b>b</b>) modified graphene and graphene oxide by chitosan.</p>
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<p>Breakthrough curves for CO<sub>2</sub> adsorbed by chitosan-modified graphene oxide with different amounts of chitosan added.</p>
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<p>Adsorption isotherms for CO<sub>2</sub> adsorbed by graphene (G) and graphene oxide (GO) and modification of them by chitosan (CTS).</p>
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<p>Breakthrough curves for CO<sub>2</sub> adsorbed by graphene (G) and graphene oxide (GO) and modification of them by chitosan (CTS).</p>
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<p>Relationship between practical and predicted adsorption uptakes for CO<sub>2</sub> adsorbed by graphene oxide modification with different dosages of chitosan.</p>
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22 pages, 1979 KiB  
Review
Methods of Capture and Transformation of Carbon Dioxide (CO2) with Macrocycles
by Edilma Sanabria, Mauricio Maldonado, Carlos Matiz, Ana C. F. Ribeiro and Miguel A. Esteso
Processes 2025, 13(1), 117; https://doi.org/10.3390/pr13010117 - 4 Jan 2025
Viewed by 801
Abstract
Rapid industrialization and the indiscriminate use of fossil fuels have generated an impact that is affecting the climate worldwide. Among the substances that are causing climate change are several gases such as carbon dioxide (CO2), methane (CH4), nitrous oxide [...] Read more.
Rapid industrialization and the indiscriminate use of fossil fuels have generated an impact that is affecting the climate worldwide. Among the substances that are causing climate change are several gases such as carbon dioxide (CO2), methane (CH4), nitrous oxide (N2O) and sulphur hexafluoride (SF6), among others. Particularly, carbon dioxide is one of the substances that has attracted the most attention from researchers, as it is responsible for more than three quarters of greenhouse gases. Because of this, many efforts have been directed towards the capture of CO2, its separation, adsorption and transformation into products that are less harmful to the environment or that even have added value in the industry. For this purpose, the use of different types of macrocycles has been explored mainly in the last 5 years. This review seeks to present the advances that have occurred in recent years in the capture and transformation of CO2 by different methods, to finally focus on the capture and transformation through macrocycle systems such as azacompounds, heterometallic macrocycles, calixpyrrols, modified cyclodextrins and metallic porphyrins, among others. Full article
(This article belongs to the Section Environmental and Green Processes)
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<p>Forms of representations of the CO<sub>2</sub> molecule.</p>
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<p>Main methods of capturing and transforming carbon dioxide.</p>
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<p>Some macrocyclic systems used in carbon dioxide fixation.</p>
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<p>Alpha-, beta- and gamma-cyclodextrins.</p>
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<p>Structure of porphyrins and metalloporphyrins.</p>
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<p>Participation of metallo-porphyrins in CO<sub>2</sub> transformation.</p>
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<p>Structure of calixarenes, resorcinarenes and pyrogallolarenes.</p>
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<p>Participation of calixarene-type systems in CO<sub>2</sub> transformation.</p>
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<p>Synthesis gas and Fisher–Tropsch process.</p>
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10 pages, 1708 KiB  
Communication
N Simultaneously Doped TiO2@Carbon Hollow Spheres with Enhanced Photocatalytic CO2 Reduction Activity
by Weiwei Fu, Ziyun Wang, Xinjie Liu and Tianjiao Li
Catalysts 2025, 15(1), 39; https://doi.org/10.3390/catal15010039 - 4 Jan 2025
Viewed by 314
Abstract
Converting carbon dioxide (CO2) into solar fuels through photocatalysis represents an appealing approach to tackling the escalating energy crisis and mitigating the greenhouse effect. In this study, using melamine–formaldehyde (MF) nanospheres as a nitrogen source, a N element was simultaneously doped [...] Read more.
Converting carbon dioxide (CO2) into solar fuels through photocatalysis represents an appealing approach to tackling the escalating energy crisis and mitigating the greenhouse effect. In this study, using melamine–formaldehyde (MF) nanospheres as a nitrogen source, a N element was simultaneously doped into the TiO2 nanoparticle structure supported by carbon hollow spheres using a one-step carbonization method to form a heterojunction N-CHS@N-TiO2 (marked as (N-(CHS@TiO2)). The composite showed superior photocatalytic activity in reducing CO2 compared with TiO2 and N-CHS: after 6 h of visible light irradiation, the CO yield was 4.3 times that of N-CHS and TiO2; 6 h of UV irradiation later, the CO yield reached 2.6 times that of TiO2 and 7 times that of N-CHS. The substantial enhancement in photocatalytic activity was attributed to the nitrogen simultaneously doped carbon hollow spheres and TiO2, mesoporous structure, small average TiO2 crystal size, large surface areas, and the heterostructure formed by N-CHS and N-TiO2. The UV-vis diffuse reflectance spectra (DRS) exhibit a significant improvement in light absorption, attributed to the visible-light-active carbon hollow sphere and the N element doping, thereby enhancing solar energy utilization. Full article
(This article belongs to the Special Issue Catalytic Properties of Hybrid Catalysts)
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Graphical abstract

Graphical abstract
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<p>XRD patterns of N-CHS, N-(CHS@TiO<sub>2</sub>), and TiO<sub>2</sub> (A: anatase, R: rutile) (<b>a</b>), TEM image of N-CHS (<b>b</b>) and N-(CHS@TiO<sub>2</sub>) (<b>c</b>), HRTEM of N-(CHS@TiO<sub>2</sub>) (<b>d</b>), the corresponding elemental mapping of C, N, O, and Ti of single N-(CHS@TiO<sub>2</sub>) (<b>e</b>), XPS survey spectra of N-CHS and N-(CHS@TiO<sub>2</sub>) (<b>f</b>), high-resolution N1s XPS profile of N-CHS and N-(CHS@TiO<sub>2</sub>) (<b>g</b>), and high-resolution XPS spectra of Ti for N-(CHS@TiO<sub>2</sub>) and TiO<sub>2</sub> (<b>h</b>).</p>
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<p>(<b>a</b>) UV-vis DRS of N-CHS, TiO<sub>2</sub> and N-(CHS@TiO<sub>2</sub>); (<b>b</b>) Tauc plots of (αhν)<sup>2</sup> versus hν; (<b>c</b>) EIS spectra of TiO<sub>2</sub>, N-CHS, and N-(CHS@TiO<sub>2</sub>); and (<b>d</b>) photocurrent of TiO<sub>2</sub>, N-CHS, and N-(CHS@TiO<sub>2</sub>).</p>
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<p>The yield of CO and CH<sub>4</sub> for N-CHS, N-(CHS@TiO<sub>2</sub>), and TiO<sub>2</sub> under visible light (<b>a</b>) and under exposure to UV light (<b>b</b>).</p>
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28 pages, 1132 KiB  
Review
Theory and Practice of Burning Solid Biofuels in Low-Power Heating Devices
by Małgorzata Dula and Artur Kraszkiewicz
Energies 2025, 18(1), 182; https://doi.org/10.3390/en18010182 - 3 Jan 2025
Viewed by 394
Abstract
Combustion is the most advanced and proven method on the market for using agricultural by-product residues and waste from the agri-food industry. Currently, a wide range of combustion technologies is used to produce heat and electricity in low-power heating devices (>50 kW) using [...] Read more.
Combustion is the most advanced and proven method on the market for using agricultural by-product residues and waste from the agri-food industry. Currently, a wide range of combustion technologies is used to produce heat and electricity in low-power heating devices (>50 kW) using various types of biofuels from biomass (woody biomass, herbaceous biomass, waste and residues from the agri-food industry). Combustion of biomass fuels, especially those of wood origin, causes lower carbon dioxide (CO2) and sulfur oxides (SOx) emissions into the atmosphere compared to coal combustion. The growing interest in solid biofuels has contributed to intensive activities on improving the combustion process and energy devices enabling effective and economic conversion of chemical energy contained in biomass into other usable forms such as heat, electricity. Having good quality fuel, it is necessary to ensure an appropriate, clean combustion technique, which allows to achieve the highest thermal efficiency of the heating device and at the same time the lowest emission of pollutants. The article presents issues related to the theory, characteristics of the combustion process and problems related to the formation of harmful chemical compounds nitrogen oxides (NOx), SOx, carbon monoxide (CO), particulate matter (PM) emitted to the atmosphere during the combustion process in low-power heating devices. The analysis indicates the possibility of minimizing undesirable phenomena during the combustion of these biofuels related to ash sintering, the formation of deposits, corrosion and improving the amount of condensable solid particles formed and therefore reducing the emission of gaseous products to the environment. Full article
(This article belongs to the Special Issue Advanced Combustion Technologies and Emission Control)
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<p>Formation mechanism of nitrogen oxides. Own study, based on [<a href="#B71-energies-18-00182" class="html-bibr">71</a>].</p>
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<p>Synergy effects between co-burned fuels [<a href="#B117-energies-18-00182" class="html-bibr">117</a>].</p>
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19 pages, 10729 KiB  
Article
Development of MEA-Based and AEP-Based CO2 Phase Change Absorbent
by Yongyan Wang, Fanghui Cheng, Jingsong Li, Yingshu Liu, Haihong Wang, Ziyi Li and Xiong Yang
Processes 2025, 13(1), 92; https://doi.org/10.3390/pr13010092 - 2 Jan 2025
Viewed by 433
Abstract
In energy conservation and low-carbon environmental protection, separating and capturing CO2 from blast furnace gas is a crucial strategy for the steel industry to achieve its dual carbon goals. This study conducts an experimental study on the phase change absorption of carbon [...] Read more.
In energy conservation and low-carbon environmental protection, separating and capturing CO2 from blast furnace gas is a crucial strategy for the steel industry to achieve its dual carbon goals. This study conducts an experimental study on the phase change absorption of carbon dioxide for the low-energy capture of carbon dioxide in blast furnace gas in iron and steel enterprises. The experiment used 30%wt monoethanolamine (MEA) and 30%wt 1-(2-aminoethyl)piperazine (AEP) as a reference to blend different absorbents, and the CO2 absorption effect of the absorbents was tested. The results indicated that the MEA system phase change absorbents have the best absorption effect when the mass ratio of additives to water is 5:5, and the AEP system has the best absorption effect at 7:3. The absorption effect of different phase separators is as follows: n-propanol > sulfolane > isopropanol. AEP/n-propanol/H2O (7:3) has a maximum absorption load of 2.03 molCO2·mol−1 amine, a relatively low rich phase ratio of 0.46, and low regeneration energy consumption. The load capacity of different absorbents was calculated based on the load experiment results, and it was found that the loading capacity of the MEA system was greater than that of the AEP system, with the maximum load capacity of MEA/n-propanol/H2O (5:5) being 4.02 mol/L. Different types of absorbents exhibited an increase in rich phase density with the increase in additive quality. The regeneration performance of the absorbent indicated that at a temperature of 393.15 K, the desorption load of n-propanol aqueous solution rich phase in the absorbent was high, and the desorption speed was the fastest. Full article
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<p>Schematic of absorption apparatus.</p>
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<p>Schematic of desorption apparatus.</p>
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<p>Schematic of CO<sub>2</sub> loading titration apparatus.</p>
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<p>Phase separation diagram of MEA/n-propanol/H<sub>2</sub>O absorbent.</p>
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<p>Diagram of the relationship between the phase separation phenomenon and the dipole moment of AEP/sulfolane/H<sub>2</sub>O absorbent (Debye is the dipole moment).</p>
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<p>Absorption loads of MEA-based absorbents with different additives at different concentrations: (<b>a</b>) MEA/n-propanol; (<b>b</b>) MEA/isopropanol; (<b>c</b>) MEA/sulfolane.</p>
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<p>Absorption rate of MEA-based absorbents with different additives at different concentrations: (<b>a</b>) MEA/n-propanol; (<b>b</b>) MEA/isopropanol; (<b>c</b>) MEA/sulfolane.</p>
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<p>Absorption load of AEP-based absorbents with different additives at different concentrations: (<b>a</b>) AEP/n-propanol; (<b>b</b>) AEP/isopropanol; (<b>c</b>) AEP/sulfolane.</p>
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<p>Absorption rate of AEP-based absorbents with different additives at different concentrations: (<b>a</b>) AEP/n-propanol; (<b>b</b>) AEP/isopropanol; (<b>c</b>) AEP/sulfolane.</p>
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<p>Desorption rate and desorption load of MEA-based absorbent with different additives (mass ratio is 5:5): (<b>a</b>) MEA/n-propanol; (<b>b</b>) MEA/isopropanol; (<b>c</b>) MEA/sulfolane.</p>
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<p>Desorption rate and desorption load of AEP-based absorbent with different additives (mass ratio is 7:3): (<b>a</b>) AEP/n-propanol; (<b>b</b>) AEP/isopropanol; (<b>c</b>) AEP/sulfolane.</p>
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<p>Density and load of MEA-based absorbent rich phase (mass ratio is 5:5): (<b>a</b>) MEA/n-propanol; (<b>b</b>) MEA/isopropanol; (<b>c</b>) MEA/sulfolane.</p>
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<p>Density and load of AEP-based absorbent rich phase (mass ratio is 7:3): (<b>a</b>) AEP/n-propanol; (<b>b</b>) AEP/isopropanol; (<b>c</b>) AEP/sulfolane.</p>
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15 pages, 841 KiB  
Article
Supercritical Extraction and Compound Profiling of Diverse Edible Mushroom Species
by Slađana Krivošija, Nataša Nastić, Milica Karadžić Banjac, Strahinja Kovačević, Sanja Podunavac-Kuzmanović and Senka Vidović
Foods 2025, 14(1), 107; https://doi.org/10.3390/foods14010107 - 2 Jan 2025
Viewed by 341
Abstract
Mushrooms are a raw material rich in many nutritional compounds, and that is why a number of them are widely known as functional food. They contain fatty acids, carbohydrates, lycopene, sterols, lovastatin, trace elements, and other valuable compounds that show a wide range [...] Read more.
Mushrooms are a raw material rich in many nutritional compounds, and that is why a number of them are widely known as functional food. They contain fatty acids, carbohydrates, lycopene, sterols, lovastatin, trace elements, and other valuable compounds that show a wide range of properties, such as hepatoprotective, anticancer, antiviral, etc. For more efficient utilisation of mushrooms’ biologically active substances, widespread supercritical carbon dioxide extraction (Sc-CO2) was used as an efficient way to isolate the high-value phytoconstituents from this type of raw material. Using Sc-CO2, the extracts of five types of edible mushrooms—Lycoperdon saccatum, Pleurotus ostreatus, Craterellus cornucopioides, Russula Cyanoxantha and Cantharellus cibarius—were obtained. During the Sc-CO2 process, the extraction time was reduced to 4 h compared to the prolonged process time applied in the typical traditional techniques (6–24 h). The extraction pressure (30 MPa) and temperature (40 °C) were constant. Fatty acids and the compounds of steroid structures were determined in the obtained extracts using GC–MS and GC–FID methods of analysis. The dominant compounds identified in the lipid extracts were fatty acids (linoleic, oleic, palmitic and stearic) and sterols (ergosterol, 7,22-ergostadienone and 7,22-ergostadienol). For complete insight into the process and to obtain the value of the extracts, chemometric analysis is provided. Principal component analysis (PCA) and hierarchical cluster analysis (HCA), as well as k-means clustering, showed that Craterellus cornucopioides was distinguished based on the extraction yield results. Full article
(This article belongs to the Section Plant Foods)
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<p>Score (<b>a</b>) and loading (<b>b</b>) plots of conducted PCA analysis covering extraction yield results.</p>
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<p>Clustered heat map (double dendrogram) of the extraction yield results.</p>
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9 pages, 3740 KiB  
Article
Ag Nanoparticle-Modified Metal Azole Framework for Enhancing the Electrocatalytic Reduction of Carbon Dioxide to Carbon Monoxide
by Xu Han, Haotian Wang, Yijie Zhang, Yuting Tan and Xiaomeng Lv
Catalysts 2025, 15(1), 32; https://doi.org/10.3390/catal15010032 - 2 Jan 2025
Viewed by 333
Abstract
The electrocatalytic reduction of carbon dioxide (CO2RR) into high-value-added products is considered to be a promising way to mitigate carbon emissions. However, it remains a challenge to design an efficient catalyst with an excellent performance. In this work, we synthesized a [...] Read more.
The electrocatalytic reduction of carbon dioxide (CO2RR) into high-value-added products is considered to be a promising way to mitigate carbon emissions. However, it remains a challenge to design an efficient catalyst with an excellent performance. In this work, we synthesized a metal azole framework (MAF) by changing 2-methylimidazole ligands into 5-mercapto-1-methyltetrazole (MMT) for use as organic linkers and mercaptan groups as anchoring sites for the Ag nanoparticles. The Ag NPs@ MAF-MMT material displayed a wide potential window from −0.6 to −1.2 V vs. RHE, with a maximum CO Faradaic efficiency (FECO) over 90.5%, and a current density of 18 mA cm−2 at −1.1 V vs. RHE for 11 h in an H-cell. This work provides a new option to immobilize Ag nanoparticles in MAFs material for the exploration of carbon dioxide reduction catalysts. Full article
(This article belongs to the Special Issue Advanced Electrocatalysts for Energy-Related Applications)
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<p>Scanning electron microscopy scan of (<b>a</b>) MAF-MMT and (<b>b</b>) AgNPs@MAF-MMT; (<b>c</b>) transmission electron microscopy scan and (<b>d</b>) high-resolution electron microscopy image of Ag NPs@MAF-MMT.</p>
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<p>(<b>a</b>) XRD patterns of MAF-MMT and Ag NPs@MAF-MMT. (<b>b</b>) FT-IR spectra of MAF-MMT and Ag NPs@MAF-MMT. The high resolution XPS spectra of (<b>c</b>) Ag 3d, (<b>d</b>) C 1s, (<b>e</b>) S 2p, and (<b>f</b>) Zn 2p in MAF-MMT and Ag NPs@MAF-MMT.</p>
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<p>(<b>a</b>) LSV, (<b>b</b>) FE<sub>CO</sub>, and (<b>c</b>) FE<sub>H2</sub> of the catalysts at different reduction potentials. (<b>d</b>) A catalytic reaction was conducted at −0.7 V vs. RHE for 11 h and CO<sub>2</sub>RR products measured at 1 h intervals. (<b>e</b>) FE<sub>CO</sub> and stability of Ag NPs@MAF-MMT compared with those of representative MOF-based catalysts [<a href="#B20-catalysts-15-00032" class="html-bibr">20</a>,<a href="#B26-catalysts-15-00032" class="html-bibr">26</a>,<a href="#B27-catalysts-15-00032" class="html-bibr">27</a>,<a href="#B28-catalysts-15-00032" class="html-bibr">28</a>,<a href="#B29-catalysts-15-00032" class="html-bibr">29</a>,<a href="#B30-catalysts-15-00032" class="html-bibr">30</a>,<a href="#B31-catalysts-15-00032" class="html-bibr">31</a>,<a href="#B32-catalysts-15-00032" class="html-bibr">32</a>].</p>
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<p>(<b>a</b>) Tafel slopes. (<b>b</b>) Nyquist plots and the equivalent circuit diagram. (<b>c</b>) Capacitance values of Ag NPs@MAF-MMT and MAF-MMT.</p>
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<p>The synthesis procedure of Ag NPs@MAF-MMT.</p>
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22 pages, 6455 KiB  
Article
Process Improvement and Economic and Environmental Evaluation of Bio-Hydrogenated Diesel Production from Refined Bleached Deodorized Palm Oil
by Amata Anantpinijwatna, Lida Simasatitkul, Kanokporn Yooyen, Suksun Amornraksa, Suttichai Assabumrungrat and Karittha Im-orb
Processes 2025, 13(1), 75; https://doi.org/10.3390/pr13010075 - 1 Jan 2025
Viewed by 773
Abstract
The co-production of BHD with other renewable fuels (i.e., using a novel process involving carbon dioxide utilization to achieve the global sustainability goal) is presented. The three configurations of BHD production from refined bleached deodorized palm oil (RBDPO), including (1) the conventional BHD [...] Read more.
The co-production of BHD with other renewable fuels (i.e., using a novel process involving carbon dioxide utilization to achieve the global sustainability goal) is presented. The three configurations of BHD production from refined bleached deodorized palm oil (RBDPO), including (1) the conventional BHD process with hydrogen recovery (BHD process), (2) the BHD process coupled with the Fischer–Tropsch process (BHD-FT process), and (3) the BHD process coupled with the bio-jet fuel and methanol processes (BHD-BIOJET-MEOH process) are investigated using the process model developed in Aspen Plus. The effect of the operating parameters is studied, and the condition of each process offering the highest BHD yield is proposed. Then, the pinch analysis and heat exchanger network (HEN) design of each proposed process are performed to find the highest energy-efficient configuration. The economic and environmental analysis is later performed to investigate the sustainability performance of each configuration. The conventional BHD process requires less hydrogen and consumes less energy than the others. The BHD-BIOJET-MEOH process is the most economically feasible, offering the highest net present value (NPV) of USD 7.93 million and the shortest payback period of 3 years and 1 month. However, it offers the highest carbon footprint of 0.820 kgCO2 eq./kg of BHD, and it presented the highest potential environmental impact (PEI) in all categories. Full article
(This article belongs to the Special Issue Process Systems Engineering for Environmental Protection)
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<p>Methodology of the process design.</p>
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<p>Block flow diagrams of (<b>a</b>) BHD process, (<b>b</b>) BHD-FT process, and (<b>c</b>) BHD-BIOJET-MEOH process.</p>
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<p>Aspen Plus model flowsheet of BHD process.</p>
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<p>Aspen Plus model flowsheet of BHD-FT process.</p>
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<p>Aspen Plus model flowsheet of BHD-BIOJET-MEOH process.</p>
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<p>Composite curves of hot and cold utility of (<b>a</b>) BHD process, (<b>b</b>) BHD-FT process, and (<b>c</b>) BHD-BIOJET-MEOH process when red line is hot utility and blue line is cold utility.</p>
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<p>HEN design diagram of BHD process.</p>
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<p>Newly designed BHD process including HEN.</p>
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<p>HEN design diagram of BHD-FT process.</p>
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<p>Newly designed BHD-FT process including HEN.</p>
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<p>HEN design diagram of BHD-BIOJET-MEOH process.</p>
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<p>Newly designed BHD-BIOJET-MEOH process including HEN.</p>
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<p>Hot and cold utility requirements before and after heat integration.</p>
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<p>Cumulative cash flow of three BHD processes.</p>
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<p>Carbon footprint of operating units and raw materials of three BHD processes.</p>
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<p>Carbon footprint of each operating unit of (<b>a</b>) BHD process, (<b>b</b>) BHD-FT process, and (<b>c</b>) BHD-BIOJET-MEOH process.</p>
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<p>Carbon footprint of each operating unit of (<b>a</b>) BHD process, (<b>b</b>) BHD-FT process, and (<b>c</b>) BHD-BIOJET-MEOH process.</p>
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<p>The environmental impact of various BHD processes in categories of (<b>a</b>) human health and (<b>b</b>) ecosystem.</p>
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<p>The environmental impact of various BHD processes in categories of (<b>a</b>) human health and (<b>b</b>) ecosystem.</p>
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14 pages, 4195 KiB  
Article
The Effect of Molten Salt Composition on Carbon Structure: Preparation of High Value-Added Nano-Carbon Materials by Electrolysis of Carbon Dioxide
by Yi Cheng, Liangxing Li, Lirong Xue, Jiahang Wu, Jingsong Wang, Xilin Huang and Chunfa Liao
Nanomaterials 2025, 15(1), 53; https://doi.org/10.3390/nano15010053 - 31 Dec 2024
Viewed by 399
Abstract
The electrochemical conversion of CO2 into high value-added carbon materials by molten salt electrolysis offers a promising solution for reducing carbon dioxide emissions. This study focuses on investigating the influence of molten salt composition on the structure of CO2 direct electroreduction [...] Read more.
The electrochemical conversion of CO2 into high value-added carbon materials by molten salt electrolysis offers a promising solution for reducing carbon dioxide emissions. This study focuses on investigating the influence of molten salt composition on the structure of CO2 direct electroreduction carbon products in chloride molten salt systems. Using CaO as a CO2 absorber, the adsorption principle of CO2 in LiCl-CaCl2, LiCl-CaCl2-NaCl and LiCl-CaCl2-KCl molten salts was discussed, and the reasons for the different morphologies and structures of carbon products were analyzed, and it was found that the electrolytic efficiency of the whole process exceeded 85%. Furthermore, cathode products are analyzed through Scanning Electron Microscope (SEM), X-Ray Diffractometer (XRD), Thermal Gravimetric Analyzer (TGA), Raman Spectra and Fourier Transform Infrared (FTIR) techniques with a focus on the content and morphology of carbon elements. It was observed that the carbon content in the carbon powder produced by molten salt electrochemical method exceeded 99%, with most carbon products obtained from electrolysis in the Li-Ca chloride molten salt system being in the form of carbon nanotubes. In contrast, the Li-Ca-K chloride system yielded carbon nanospheres, while a mixture was found in the Li-Ca-Na chloride system. Therefore, experimental results demonstrate that altering the composition of the system allows for obtaining the desired product size and morphology. This research presents a pathway to convert atmospheric CO2 into high value-added carbon products. Full article
(This article belongs to the Special Issue Nanomaterials for Sustainable Green Energy)
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<p>(<b>a</b>) The thermodynamic data of the reaction between CaO and CO<sub>2</sub> calculated using HSC software. (<b>b</b>) Binary phase diagram of CaCl<sub>2</sub>-LiCl from Factsage.</p>
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<p>(<b>a</b>) The products attached to the Ni electrode after electrolysis. (<b>b</b>) The product subsequent to acid leaching and purification treatment (on the right is a schematic diagram of the structure of CNTs using C4D). (<b>c</b>) SEM map and element distribution obtained after purification.</p>
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<p>Cyclic voltammetry curve recorded at 750 °C at scanning speed of 10 mV/s using Ni wire as working electrode, carbon rod as counter electrode, Pt wire as reference electrode, (<b>a</b>) LiCl-CaCl<sub>2</sub> system in Ar atmosphere, (<b>b</b>) LiCl-CaCl<sub>2</sub> system in CO<sub>2</sub> atmosphere.</p>
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<p>SEM image of the product obtained from electrolysis of CO<sub>2</sub> in LiCl-CaCl<sub>2</sub> molten salt at 750 °C, the magnifications are (<b>a</b>) 2000 times; (<b>b</b>) 10,000 times; (<b>c</b>) 50,000 times; (<b>d</b>) 20,000 times.</p>
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<p>At 750 °C, the system was electrolyzed at a constant current of 200 mA/cm<sup>2</sup>: (<b>a</b>) SEM images of the products obtained from electrolysis of CO<sub>2</sub> in LiCl-NaCl molten salt, (<b>b</b>,<b>c</b>) SEM images of the products obtained from electrolysis of CO<sub>2</sub> in LiCl-CaCl<sub>2</sub>-NaCl molten salt, (<b>d</b>) SEM images of the products obtained from electrolysis of CO<sub>2</sub> in LiCl-KCl molten salt, (<b>e</b>,<b>f</b>) SEM images of the products obtained from electrolysis of CO<sub>2</sub> in LiCl-CaCl<sub>2</sub>-KCl molten salt.</p>
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<p>The outer diameter distribution of products obtained at a current of 200 mA/cm<sup>2</sup> and 750 °C under different electrolyte systems: (<b>a</b>) CNTs in Li-CaCl<sub>2</sub> and CNTs in Li-CaCl<sub>2</sub>-NaCl, (<b>b</b>) CSs in Li-CaCl<sub>2</sub>-KCl and CSs in Li-CaCl<sub>2</sub>-NaCl.</p>
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<p>The XRD diagram of the product obtained by (<b>a</b>) LiCl-CaCl<sub>2</sub>, (<b>b</b>) LiCl-CaCl<sub>2</sub>-NaCl, (<b>c</b>) LiCl-CaCl<sub>2</sub>-KCl and its corresponding unit cell type and parameters in 750 °C at a current of 200 mA/cm<sup>2</sup>.</p>
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<p>The TG-DTG thermograms of carbon materials, recorded at a heating rate of 10 °C/min at a low air velocity of 100 milliliters per minute: (<b>a</b>) CNTs, (<b>b</b>) CSs.</p>
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<p>FTIR spectra of CNT and CS.</p>
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<p>Raman characterization of products in different systems under He-Ne laser wavelength of 532 nm. Raman spectra of electrolytic products in different systems; 1 and 2 are in LiCl-CaCl<sub>2</sub> system, 3 and 4 are in LiCl-CaCl<sub>2</sub>-NaCl system, 5 and 6 are in LiCl-CaCl<sub>2</sub>-KCl.</p>
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15 pages, 2061 KiB  
Article
Kinetics of Supercritical CO2 Extraction from Burrito (Aloysia polystachya) Leaves and Sucupira-Preta (Bowdichia virgilioides) Seeds
by Gabrielle Vaz Vieira, Michel Rubens dos Reis Souza, Carlos Toshiyuki Hiranobe, José Eduardo Goncalves, Cristiane Mengue Feniman Moritz, Otávio Akira Sakai, Leila Maria Sotocorno e Silva, Michael Jones da Silva, Erivaldo Antônio da Silva, Renivaldo José dos Santos, Edson Antônio da Silva, Lucio Cardozo-Filho and Leandro Ferreira-Pinto
Separations 2025, 12(1), 6; https://doi.org/10.3390/separations12010006 - 31 Dec 2024
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Abstract
This study investigated the application of supercritical carbon dioxide (CO2) for the extraction of essential oils from plant materials with anxiolytic potential, focusing on the leaves of burrito (Aloysia polystachya) and the seeds of sucupira-preta (Bowdichia virgilioides). [...] Read more.
This study investigated the application of supercritical carbon dioxide (CO2) for the extraction of essential oils from plant materials with anxiolytic potential, focusing on the leaves of burrito (Aloysia polystachya) and the seeds of sucupira-preta (Bowdichia virgilioides). The supercritical extraction technique was chosen for its ability to produce high-purity extracts without residual solvents and to reduce the environmental impact. This study evaluated the influence of temperature (40 °C, 50 °C, and 60 °C) and pressure (22 MPa, 25 MPa, and 28 MPa) on extraction efficiency using a 22 factorial design with triplicates at the central point. The maximum yields were 1.2% for burrito leaves and 4.2% for sucupira-preta seeds. Despite their relatively low yields, the extracts contained a diverse range of chemical compounds, including fatty acids (oleic, linoleic, and palmitic acids), squalene, β-carotene, vitamin E, and other bioactive molecules with antioxidant, anti-inflammatory, and immunomodulatory properties. Statistical analysis demonstrated that pressure was the most influential factor affecting yield, whereas temperature played a secondary role. The Sovová kinetic model provided a good fit for the extraction curves, with determination coefficients (R2) above 0.95, thus validating the efficiency of the method. These results highlight the pharmaceutical potential of these extracts, particularly for therapeutic and anxiolytic purposes. Full article
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Figure 1

Figure 1
<p>A schematic of the experimental supercritical extraction unit: 1—CO<sub>2</sub> cylinder; 2—syringe pump; 3—thermostatic bath; 4—pressure indicator; 5—temperature controller/indicator; 6—extractor; 7—valve; 8—needle-type valve attached to an aluminum jacket for heating; 9—thermostatic bath; 10—aluminum structure.</p>
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<p>Experimental kinetic extraction curves with supercritical CO<sub>2</sub> fitted using the Sovová model (<span class="html-fig-inline" id="separations-12-00006-i001"><img alt="Separations 12 00006 i001" src="/separations/separations-12-00006/article_deploy/html/images/separations-12-00006-i001.png"/></span>) of burrito leaves: 40 °C (■, 22 MPa; ▲, 28 MPa); 50 °C (<span class="html-fig-inline" id="separations-12-00006-i002"><img alt="Separations 12 00006 i002" src="/separations/separations-12-00006/article_deploy/html/images/separations-12-00006-i002.png"/></span>, 25 MPa); 60 °C (●, 22 MPa; ▼, 28 MPa) with a constant flow rate of 2.0 mL min<sup>−1</sup>.</p>
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<p>Experimental kinetic extraction curves with supercritical CO<sub>2</sub> fitted using Sovová model (<span class="html-fig-inline" id="separations-12-00006-i001"><img alt="Separations 12 00006 i001" src="/separations/separations-12-00006/article_deploy/html/images/separations-12-00006-i001.png"/></span>) of sucupira-preta seeds: 40 °C (■, 22 MPa; ▲, 28 MPa); 50 °C (<span class="html-fig-inline" id="separations-12-00006-i002"><img alt="Separations 12 00006 i002" src="/separations/separations-12-00006/article_deploy/html/images/separations-12-00006-i002.png"/></span>, 25 MPa); 60 °C (●, 22 MPa; ▼, 28 MPa) with a constant flow rate of 2.0 mL min<sup>−1</sup>.</p>
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<p>A response surface plot illustrating the extraction yield of oil from burrito leaves as a function of temperature and pressure, with a constant flow rate of 2.0 mL min<sup>−1</sup>.</p>
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<p>A response surface plot showing the oil extraction yield from sucupira-preta seeds as influenced by temperature and pressure at a fixed flow rate of 2.0 mL min<sup>−1</sup>.</p>
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<p>Pareto chart: analysis of linear effects of variables. (<b>A</b>) Burrito leaves and (<b>B</b>) sucupira-preta seeds.</p>
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