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Structure and Mixed Proton-Electronic Conductivity in PR-Substituted La5.4MoO12- Ceramics
Abraham Sánchez-Caballero,
José M. Porras-Vázquez,
Lucía dos Santos-Gómez,
Javier Zamudio-García,
Antonia Infantes-Molina,
Jesús Canales-Vázquez,
Enrique R. Losilla,
David Marrero-López
Posted: 30 December 2024
In Vitro Bacterial Growth on Titanium Surfaces Treated with Nanosized Hydroxyapatite
Maria Holmström,
Sonia Esko,
Karin Danielsson,
Per Kjellin
Posted: 30 December 2024
Simultaneous Determination of Six Acidic Herbicides and Metabolites in Plant Origin Matrices by QuEChERS-HPLC-MS/MS
Qiqi Jin,
Qianwen Xu,
Zhiyong Zhao,
Wenshuai Si,
Bing Bai,
Lei Chen,
Changyan Zhou
Posted: 30 December 2024
Reducing Oxidation in the Aspire Oil Biodiesel-diesel Blends: Metal Deactivators as Antioxidant Schiff Base Derivatives
Nalan Türköz Karakullukçu
Posted: 30 December 2024
Procedures for XRD Phase Analysis: The Case of Fine Sediments from Peña Blanca, Chihuahua, Mexico
Carmen del Rocio Caraveo-Castro,
Yair Rodríguez-Guerra,
Luis Fuentes-Montero,
Luis E. Fuentes-Cobas,
María Elena Montero-Cabrera
Posted: 30 December 2024
Composition of EETP801 Cocoa Powder, a Native Amazonian Cocoa Cultivar Grown Under Sustainable Organic Conditions
Rocío De la Peña-Armada,
Roberta Ascrizzi,
Rocio Alarcon,
Michelle Viteri,
Guido Flamini,
Jose M. Prieto
In this study, we have analysed the Amazonian variety EETP801 Cacao, grown under sustainable organic conditions, in comparison to CCN51 cacao grown on a neighbouring commercial farm using standard practices and an European commercial cacao powdered beverage. The overall metabolite profile was analysed by high performance TLC analyses (HPTLC), the volatile fraction by head-space gas chromatography–mass spectrometry (HS-GC-MS) and the xanthine alkaloids by quantitative liquid chromatography-UV photodiode array (HPLC-DAD) analyses. Total polyphenol content was determined by the Folin-Ciocalteu method. Despite the reduced production of cocoa by the EETP801 cultivar in comparison with the CCN51 cultivar, the obtained produce is significantly richer in theobromine (130 mg vs 170 mg per g of cacao) with CCN51 having double concentration of theophylline (12.6 vs 6.5 mg per g of cacao). Qualitatively, EETP-801 has the same polyphenolic composition (as per the HPTLC fingerprint) of the CCN51 cultivar but shows more traces of glycosylated flavonoids (rutin). The HS-GC-MS analyses revealed that the fragrance of both Amazonian cacao samples was superior to that of the commercial sample. The variability in the artisan fermentation and roasting processes influenced certain aspects of the volatile composition. The cultivar EETP801 is a viable option for a more ecologically conscious sector of the cocoa beverages consumer group.
In this study, we have analysed the Amazonian variety EETP801 Cacao, grown under sustainable organic conditions, in comparison to CCN51 cacao grown on a neighbouring commercial farm using standard practices and an European commercial cacao powdered beverage. The overall metabolite profile was analysed by high performance TLC analyses (HPTLC), the volatile fraction by head-space gas chromatography–mass spectrometry (HS-GC-MS) and the xanthine alkaloids by quantitative liquid chromatography-UV photodiode array (HPLC-DAD) analyses. Total polyphenol content was determined by the Folin-Ciocalteu method. Despite the reduced production of cocoa by the EETP801 cultivar in comparison with the CCN51 cultivar, the obtained produce is significantly richer in theobromine (130 mg vs 170 mg per g of cacao) with CCN51 having double concentration of theophylline (12.6 vs 6.5 mg per g of cacao). Qualitatively, EETP-801 has the same polyphenolic composition (as per the HPTLC fingerprint) of the CCN51 cultivar but shows more traces of glycosylated flavonoids (rutin). The HS-GC-MS analyses revealed that the fragrance of both Amazonian cacao samples was superior to that of the commercial sample. The variability in the artisan fermentation and roasting processes influenced certain aspects of the volatile composition. The cultivar EETP801 is a viable option for a more ecologically conscious sector of the cocoa beverages consumer group.
Posted: 30 December 2024
Construction of ZnO/r-GO Composite Photocatalyst for Improved Photodegration Organic Pollutants
Yun Ding,
Wenzhen Qin,
Huihua Zhu,
Yuhua Dai,
Xiaowei Hong,
Suqin Han,
Yu Xie
In this work, the simple hydrothermal method was used to prepare a series of ZnO /r-GO (ZGO-x) catalysts. The obtained products were subjected by a series of characterization, which showed that The zinc oxide particles were encapsulated on r-GO and the crystal structure was not disrupted. In addition, due to the large specific surface area and the good electrical conductivity of r-GO, more photogenerated electrons are rapidly transferred to the r-GO surface to participate in the reaction, thus improving the photocatalytic performance. The degradation rate of sample ZGO-3 reached 100% for RhB after simulated sunlight irradiation for 150 min, whereas the pure ZnO degraded RhB by about 83% under the same environment. The ZGO-3 also showed the best photocatalytic degradation of methyl orange, with 100% degradation in 180 min, whereas pure ZnO degraded only 87.64% of methyl orange under solar irradiation.
In this work, the simple hydrothermal method was used to prepare a series of ZnO /r-GO (ZGO-x) catalysts. The obtained products were subjected by a series of characterization, which showed that The zinc oxide particles were encapsulated on r-GO and the crystal structure was not disrupted. In addition, due to the large specific surface area and the good electrical conductivity of r-GO, more photogenerated electrons are rapidly transferred to the r-GO surface to participate in the reaction, thus improving the photocatalytic performance. The degradation rate of sample ZGO-3 reached 100% for RhB after simulated sunlight irradiation for 150 min, whereas the pure ZnO degraded RhB by about 83% under the same environment. The ZGO-3 also showed the best photocatalytic degradation of methyl orange, with 100% degradation in 180 min, whereas pure ZnO degraded only 87.64% of methyl orange under solar irradiation.
Posted: 30 December 2024
Optimizing Methane Oxidative Coupling over La2O3: Kinetic and Product Analysis
Zhehao Qiu,
Yulu Cai
Posted: 27 December 2024
The Influence of Water Vapor and Module Modes on the Membrane-Based Post-Combustion CO2 Capture: A Simulation Approach
Daria Miroshnichenko,
Maxim Shalygin,
Stepan Bazhenov
Despite the development of nuclear and alternative energy, thermal power plants operating by burning fossil fuels (coal, petroleum products or natural gas) will retain a significant share in the energy balance for a long time. In this regard, it is of particular interest to reduce CO2 emissions from the combustion of organic fuels through its capture and subsequent use or burial. In our work, mathematical modeling of the two-stage process of membrane extraction of CO2 from the flue gases of a thermal power plant was carried out, taking into account the presence of water vapor and various operating modes of the membrane module. We used commercially available polymer membranes for gas separation in our simulations. The calculations showed: Taking into account the presence of water vapor makes it possible to reduce the required membrane area by 1.6 times; For the degree of CO2 extraction < 80% in one stage, cross-flow and counter-current modes provide equal indicators for the required membrane area, and the co-current mode turns out to be less advantageous already with a degree of CO2 extraction > 60%. In this regard, in the area of low CO2 extraction values at the first stage, any flow organization mode in the membrane module can be selected, and in the high area, a counter-current has a slight advantage over the cross-flow mode; An optimal combination of membrane areas in the first and second stages is shown to achieve the maximum CO2 concentration in the product stream; Polaris Gen-2 membranes provide the best performance after two-stage separation: the CO2 content in the product stream was > 85 mol% and > 90 mol% with a total recovery rate of 80 and 50%, respectively; PolyActive and PPO membranes provide equal indicators for the CO2 content in the product stream, but in the use of PolyActive, the required membrane area is 2.3 times less.
Despite the development of nuclear and alternative energy, thermal power plants operating by burning fossil fuels (coal, petroleum products or natural gas) will retain a significant share in the energy balance for a long time. In this regard, it is of particular interest to reduce CO2 emissions from the combustion of organic fuels through its capture and subsequent use or burial. In our work, mathematical modeling of the two-stage process of membrane extraction of CO2 from the flue gases of a thermal power plant was carried out, taking into account the presence of water vapor and various operating modes of the membrane module. We used commercially available polymer membranes for gas separation in our simulations. The calculations showed: Taking into account the presence of water vapor makes it possible to reduce the required membrane area by 1.6 times; For the degree of CO2 extraction < 80% in one stage, cross-flow and counter-current modes provide equal indicators for the required membrane area, and the co-current mode turns out to be less advantageous already with a degree of CO2 extraction > 60%. In this regard, in the area of low CO2 extraction values at the first stage, any flow organization mode in the membrane module can be selected, and in the high area, a counter-current has a slight advantage over the cross-flow mode; An optimal combination of membrane areas in the first and second stages is shown to achieve the maximum CO2 concentration in the product stream; Polaris Gen-2 membranes provide the best performance after two-stage separation: the CO2 content in the product stream was > 85 mol% and > 90 mol% with a total recovery rate of 80 and 50%, respectively; PolyActive and PPO membranes provide equal indicators for the CO2 content in the product stream, but in the use of PolyActive, the required membrane area is 2.3 times less.
Posted: 27 December 2024
Sputter Deposition and Nanoindentation of FeNiCoCrCu High Entropy Alloy coating: A Molecular Dynamics Study
Sriram Anand,
Natraj Yedla,
Vaduganathan Karthik
Posted: 27 December 2024
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