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Alternative Catalytic Reactors for CO2 Hydrogenation to Liquid Fuels
Simona Renda,
Miguel Menéndez
Posted: 16 April 2025
Study on the Combustion Behavior and Kinetic Characteristics of Semi-Coke from Oil Shale
Fajun Zhao,
Lei Zhang,
Sen Liu,
Tianyu Wang,
Peiyong Xue,
Ming Xuan Wu,
Jiankang Yun
Posted: 09 April 2025
Mechanisms and Optimization of Foam Flooding in Heterogeneous Thick Oil Reservoirs: Insights from Large-Scale 2D Sandpack Experiments
Qingchun Meng,
Hongmei Wang,
Weiyou Yao,
Yuyang Han,
Xianqiu Chao,
Tairan Liang,
Yongxian Fang,
Wenzhao Sun,
Huabin Li
Posted: 08 April 2025
Perspectives on Circular Economy and Efficient Resource Utilization of Valorized Value-Added Material for Sustainable Development
Kingsley Igenepo John,
Adeleye Timothy Adeleye,
Sehrish Munsif,
Babatope Oluseun Odusina,
Prof. Martins O. Omorogie
Posted: 07 April 2025
Optimal Experiments for Hybrid Modeling of Methanol Synthesis Kinetics
Lothar Kaps,
Johannes Leipold,
Christoph Plate,
Carl Julius Martensen,
Wieland Kortuz,
Andreas Seidel-Morgenstern,
Achim Kienle,
Sebastian Sager
Posted: 04 April 2025
Novel Aspects in Drive Train Tribology
Mario Brito,
Joerg Fliege,
Fiddelaers Frank,
Wranik Juergen,
Goerlach Bernd,
Holweger Walter
Posted: 01 April 2025
Preparation of V₂O₅ Composite Cathode Material Based on In-Situ Intercalated Polyaniline and Its High-Performance Aqueous Zinc-Ion Battery Applications
Shilin Li,
Taoyun Zhou,
Yun Cheng,
Xinyu Li
Posted: 30 March 2025
Contribution of Sessile Acidophiles on Chalcopyrite Bioleaching under Controlled Redox Potentials
Qiru Yang,
Yan Jia,
Luohu Zhang,
Qiaoyi Tan,
Heyun Sun,
Jiaqi Jin,
Jingkui Qu,
Renman Ruan,
Chao Zhang
Posted: 17 March 2025
Optimizing Silage Efficiency: The Role of Ryegrass Varieties, Harvest Time, and Additives in Enhancing Perennial Ryegrass (Lolium perenne) Fermentation
Tianyi Guo,
Tong Niu,
Katrin Kuka,
Nils Tippkötter
The increasing demand for bio-based chemicals and sustainable materials has placed biomass-derived lactic acid in the spotlight as a key building block for biodegradable polylactic acid (PLA). Perennial ryegrass (Lolium perenne) is a promising feedstock due to its high dry matter (DM) yield, adaptability, and widespread agricultural use. This study investigates an integrated lactic acid–silage cascade process, focusing on how pH regulation, harvest timing, and biomass characteristics influence lactic acid production while maintaining agronomic efficiency. The results highlighted the crucial role of pH management and silage duration in optimizing lactic acid production. A silage period of 21 days was found to be optimal, as peak lactic acid yields were consistently observed at this stage. Maintaining a pH range of 4.5 to 6 proved essential for stabilizing fermentation, with citrate buffering at pH 6 leading to the highest lactic acid yields and minimizing undesirable by-products. Harvest timing also significantly affected lactic acid yield per hectare. While later harvesting increased total DM yield, it led to a decline in lactic acid concentration per kg DM. Tetraploid ryegrass (Explosion) maintained stable lactic acid yields due to higher biomass accumulation, whereas diploid varieties (Honroso) experienced a net reduction. From an agronomic perspective, optimizing harvest timing and variety selection is key to balancing biomass yield and fermentation efficiency. While tetraploid varieties offer greater flexibility, diploid varieties require precise harvest timing to avoid losses. These findings contribute to sustainable forage management, improving lactic acid production, silage efficiency, and agricultural resource use.
The increasing demand for bio-based chemicals and sustainable materials has placed biomass-derived lactic acid in the spotlight as a key building block for biodegradable polylactic acid (PLA). Perennial ryegrass (Lolium perenne) is a promising feedstock due to its high dry matter (DM) yield, adaptability, and widespread agricultural use. This study investigates an integrated lactic acid–silage cascade process, focusing on how pH regulation, harvest timing, and biomass characteristics influence lactic acid production while maintaining agronomic efficiency. The results highlighted the crucial role of pH management and silage duration in optimizing lactic acid production. A silage period of 21 days was found to be optimal, as peak lactic acid yields were consistently observed at this stage. Maintaining a pH range of 4.5 to 6 proved essential for stabilizing fermentation, with citrate buffering at pH 6 leading to the highest lactic acid yields and minimizing undesirable by-products. Harvest timing also significantly affected lactic acid yield per hectare. While later harvesting increased total DM yield, it led to a decline in lactic acid concentration per kg DM. Tetraploid ryegrass (Explosion) maintained stable lactic acid yields due to higher biomass accumulation, whereas diploid varieties (Honroso) experienced a net reduction. From an agronomic perspective, optimizing harvest timing and variety selection is key to balancing biomass yield and fermentation efficiency. While tetraploid varieties offer greater flexibility, diploid varieties require precise harvest timing to avoid losses. These findings contribute to sustainable forage management, improving lactic acid production, silage efficiency, and agricultural resource use.
Posted: 11 March 2025
Research on Indoor Experimental Technology of Ultra-High Temperature Acidizing Corrosion Inhibitors Containing N-Heterocyclic Quaternary Ammonium Salts
Xinghua Zhang
Posted: 06 March 2025
Exploring the Performance Advantages of p-Aminobenzenesulfonate-Based Zwitterionic Gemini Surfactants in Oil Recovery
Zhaozheng Song,
Shiyuan Xia,
Tongji Yang,
Zhihong Li,
Jiayi Li
Posted: 03 March 2025
Activated Carbons as Supports for Sulfided Mo-Based Catalysts Intended for the Hydroprocessing of Lipidic Feedstocks
Antonio M. de Freitas Junior,
Ruana D. Brandão,
Jeremie Garnier,
Myller S. Tonhá,
Wagner da N Mussel,
Daniel Ballesteros Plata,
Enrique Rodríguez-Castellón,
Marcos Juliano Prauchner
Posted: 28 February 2025
The Effect of Fusion Temperature, Aging Time and Aging Temperature to the Water Adsorbent Synthesized from Spent Bleaching Earth to Purify Ethanol-Water Mixture
Norshida Abdul Kadir
Water adsorbent to dehydrate water ethanol mixture was synthesized from spent bleaching earth (SBE) using modified fusion method. The SBE was regenerated by heat at 750C. Alumina (Al2O3) was added to SBE with 80 g alumina per 100 g SBE. Potassium hydroxide (KOH) was added to SBE with stoichiometry ratio of KOH: SBE of 1.1 then mixed and fused at temperature 650C and 550C for 12 hours in a furnace. The fused mixture was grounded and mixed with water at 65 g H2O per 100 g SBE. This mixture was aged at 60C and 80C in an oven before crystallization took place in 5 parts by weight 5% KOH for 48 hours. The product obtained was washed 3 times with distilled water using filtration set and dried in oven at 220C for 20 hours. Full multilevel factorial experiments were carried out. Analysis of the results by using Minitab Release 14 Statistical software revealed that the main effect of fusion temperature and aging time was significant. The analysis also showed that there was significant interaction effect of fusion temperature to aging time and aging temperature. The best conditions to synthesize the water adsorbent were: 550°C of fusion temperature, 80°C of aging temperature and 3 days of aging time with water uptake of 0.0353 g H2O / g water adsorbent, approximately to 84% of commercialized of zeolite 3A.
Water adsorbent to dehydrate water ethanol mixture was synthesized from spent bleaching earth (SBE) using modified fusion method. The SBE was regenerated by heat at 750C. Alumina (Al2O3) was added to SBE with 80 g alumina per 100 g SBE. Potassium hydroxide (KOH) was added to SBE with stoichiometry ratio of KOH: SBE of 1.1 then mixed and fused at temperature 650C and 550C for 12 hours in a furnace. The fused mixture was grounded and mixed with water at 65 g H2O per 100 g SBE. This mixture was aged at 60C and 80C in an oven before crystallization took place in 5 parts by weight 5% KOH for 48 hours. The product obtained was washed 3 times with distilled water using filtration set and dried in oven at 220C for 20 hours. Full multilevel factorial experiments were carried out. Analysis of the results by using Minitab Release 14 Statistical software revealed that the main effect of fusion temperature and aging time was significant. The analysis also showed that there was significant interaction effect of fusion temperature to aging time and aging temperature. The best conditions to synthesize the water adsorbent were: 550°C of fusion temperature, 80°C of aging temperature and 3 days of aging time with water uptake of 0.0353 g H2O / g water adsorbent, approximately to 84% of commercialized of zeolite 3A.
Posted: 17 February 2025
Research of the Process of Obtaining Monocalcium Phosphate from Unconditional Phosphate Raw Materials
Abibulla Anarbayev,
Balzhan Kabylbekova,
Zhakhongir Khussanov,
Bakyt Smailov,
Nurlan Anarbaev,
Yevgeniy Kulikov
Posted: 13 February 2025
Kinetic Investigation of Dissolution of Sb2S3 in Na2S and NaOH Alkaline Media
Milad Rahimian,
Eskandar Keshavarz Alamdari,
Sadegh Firoozi
Posted: 22 January 2025
Matrix Reforming of Hydrocarbons: New Possibilities For Low-Tonnage Gas Processing and Energy
Vladimir Arutyunov,
Valery Savchenko,
Aleksey Nikitin,
Igor V. Sedov
Posted: 20 January 2025
Valorization of Spend Coffee Grounds Using Koh and Concentrated Leachate as Activating Agents in Slow Pyrolysis at 600ºC – a Comparative Analysis of Char Properties
Ronei de Almeida,
Marcelo Mendes Vianna,
Francesco Lanero,
Maria Cristina Lavagnolo,
Paolo Sgarbossa,
Roberta Bertani,
Bianca Ramalho Quintaes,
Daniele Maia Bila,
Juacyara Carbonelli Campos
Posted: 13 January 2025
Harvesting Salinity Gradient Energy by Diffusion of Ions, Liquid Water and Water Vapor
Joost Veerman
Posted: 08 January 2025
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
Influence of Added Cellulose Nanocrystals on the Rheology of Polymers
Rajinder Pal,
Parth Deshpande,
Smit Patel
Posted: 13 December 2024
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