Pub Date : 2025-12-11DOI: 10.1016/j.partic.2025.11.020
Kaize Shi , Ali Hassanpour , Meisam Babaie , Masoud Jabbari
Material extrusion is a key step in the solvent-free fabrication of lithium-ion battery (LIB) electrodes, offering reduced costs and environmental impact compared to slurry-based methods. While discrete element method (DEM) based mesoscopic models have been used to study twin-screw extrusion, the microstructural characterisation of extrudates immediately after nozzle exit remains unexplored. In this study, a series of DEM simulations were conducted to perform a sensitivity analysis of the microstructure and electrochemical performance-related parameters of extruded electrode filaments by varying the feeding rate and feeding mode, screw rotational speed, and particle cohesion. Furthermore, this work addresses the previously unexamined phenomenon of filament expansion during extrusion. By introducing the Augmented Dickey-Fuller (ADF) method, the study also provides the first analysis of the temporal dynamic stability of filament quality during the dry electrode manufacturing extrusion process. The results show that increasing the screw speed from 100 to 500 RPM reduces porosity by 10 % and limits expansion, while lower speeds improve consistency in electrode quality. A novel approach to quantifying dynamic behaviour is proposed, offering insights for optimising solvent-free electrode manufacturing.
{"title":"Modelling of dry manufacturing of LFP cathode filaments with twin-screw extruder using the Discrete Element Method","authors":"Kaize Shi , Ali Hassanpour , Meisam Babaie , Masoud Jabbari","doi":"10.1016/j.partic.2025.11.020","DOIUrl":"10.1016/j.partic.2025.11.020","url":null,"abstract":"<div><div>Material extrusion is a key step in the solvent-free fabrication of lithium-ion battery (LIB) electrodes, offering reduced costs and environmental impact compared to slurry-based methods. While discrete element method (DEM) based mesoscopic models have been used to study twin-screw extrusion, the microstructural characterisation of extrudates immediately after nozzle exit remains unexplored. In this study, a series of DEM simulations were conducted to perform a sensitivity analysis of the microstructure and electrochemical performance-related parameters of extruded electrode filaments by varying the feeding rate and feeding mode, screw rotational speed, and particle cohesion. Furthermore, this work addresses the previously unexamined phenomenon of filament expansion during extrusion. By introducing the Augmented Dickey-Fuller (ADF) method, the study also provides the first analysis of the temporal dynamic stability of filament quality during the dry electrode manufacturing extrusion process. The results show that increasing the screw speed from 100 to 500 RPM reduces porosity by 10 % and limits expansion, while lower speeds improve consistency in electrode quality. A novel approach to quantifying dynamic behaviour is proposed, offering insights for optimising solvent-free electrode manufacturing.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"109 ","pages":"Pages 1-11"},"PeriodicalIF":4.3,"publicationDate":"2025-12-11","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145750044","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-10DOI: 10.1016/j.partic.2025.12.004
Saikat Barua , Mohammad Zulafif Bin Rahim , Qingqing Liu
Given the growing emphasis on sustainable industrial practices and regulatory constraints on particulate emissions, enhancing cyclone separator performance remains a critical area of research for ensuring the high-efficient solid-gas separation with minimal energy penalties. This study presents a comprehensive numerical investigation and multi-objective optimisation of a dual-inlet cyclone separator to enhance the particle collection efficiency while minimizing the pressure drop. The Eulerian-Lagrangian approach is employed using the RNG turbulence modelling, coupled with the Discrete Phase Model for particle tracking. Key geometric parameters, including the inlet height to width, vortex finder angle, vortex finder diameter, barrel height, cone height, and bin diameter, are systematically varied to analyse their effects on the cyclone performance. Two optimal factors are tested among the three most significant factors at once to evaluate their combined effects on the collection efficiency and the pressure drop. Results indicate that the optimised cyclone design improves average collection efficiency by 11.5 % across particle sizes, reduces the Euler number by 50.96 %, and lowers the particle cut-off diameter by 16.15 %, while maintaining a balanced trade-off with the pressure drop. The prediction errors for the pressure drop and the collection efficiency are within acceptable limits at 11 % and 3.5 %, respectively. The improved geometry strengthens the tangential flow and moderates the peak axial velocity, resulting in a more effective centrifugal separation for fine particles.
{"title":"Multi-objective optimisation of dual inlet cyclone separator using response surface methodology","authors":"Saikat Barua , Mohammad Zulafif Bin Rahim , Qingqing Liu","doi":"10.1016/j.partic.2025.12.004","DOIUrl":"10.1016/j.partic.2025.12.004","url":null,"abstract":"<div><div>Given the growing emphasis on sustainable industrial practices and regulatory constraints on particulate emissions, enhancing cyclone separator performance remains a critical area of research for ensuring the high-efficient solid-gas separation with minimal energy penalties. This study presents a comprehensive numerical investigation and multi-objective optimisation of a dual-inlet cyclone separator to enhance the particle collection efficiency while minimizing the pressure drop. The Eulerian-Lagrangian approach is employed using the RNG <span><math><mrow><mi>k</mi><mo>-</mo><mi>ε</mi></mrow></math></span> turbulence modelling, coupled with the Discrete Phase Model for particle tracking. Key geometric parameters, including the inlet height to width, vortex finder angle, vortex finder diameter, barrel height, cone height, and bin diameter, are systematically varied to analyse their effects on the cyclone performance. Two optimal factors are tested among the three most significant factors at once to evaluate their combined effects on the collection efficiency and the pressure drop. Results indicate that the optimised cyclone design improves average collection efficiency by 11.5 % across particle sizes, reduces the Euler number by 50.96 %, and lowers the particle cut-off diameter by 16.15 %, while maintaining a balanced trade-off with the pressure drop. The prediction errors for the pressure drop and the collection efficiency are within acceptable limits at 11 % and 3.5 %, respectively. The improved geometry strengthens the tangential flow and moderates the peak axial velocity, resulting in a more effective centrifugal separation for fine particles.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"109 ","pages":"Pages 45-58"},"PeriodicalIF":4.3,"publicationDate":"2025-12-10","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145789191","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
The utilization of granite powder (GP) is substantially limited by its low pozzolanic activity and inert structure, posing a significant challenge for its high-volume incorporation. This study conducts experimental research on cold-bonded ceramsite based on the GP–fly ash–cement system, adopting the modified Andreasen–Andersen (MAA) particle packing model as a tool for mix ratio design and evaluation. By designing multiple groups of different particle size combinations, the raw material particle gradation is made to produce controllable deviations from the MAA target curve within a certain range. RSS is used to quantitatively characterize the degree of deviation of the particle gradation from the MAA target curve, and the influence mechanism of this deviation on the physical properties and pore structure of ceramsite is systematically analyzed. The results indicated that an RSS value of 6736 yielded the most compact ceramsite structure, which exhibited a cylinder compressive strength of 5.76 MPa, a bulk density of 1041 kg/m3, and a water absorption as low as 12.65 %. Further particle size fractionation experiments revealed that single-size raw material systems performed significantly worse than full-range particle distributions. The latter facilitated the formation of a skeleton–filler collaborative structure, thereby enhancing compactness and mechanical stability. Compared with existing utilization pathways of GP, the proposed structure-regulated preparation strategy for cold-bonded ceramsite enables up to 85 % incorporation of GP and delivers comprehensive performance improvement without reliance on high-temperature sintering or alkali activation. This approach demonstrates considerable engineering feasibility and application potential, providing a novel perspective and theoretical foundation for the high-efficiency valorization of low-activity solid wastes.
{"title":"Preparation of cold-bonded ceramsite based on particle packing theory and high-efficiency utilization of granite powder","authors":"Hongqiang Li, Hui Li, Yueyao Zhao, Hongbo Cui, Wukui Zheng","doi":"10.1016/j.partic.2025.12.002","DOIUrl":"10.1016/j.partic.2025.12.002","url":null,"abstract":"<div><div>The utilization of granite powder (GP) is substantially limited by its low pozzolanic activity and inert structure, posing a significant challenge for its high-volume incorporation. This study conducts experimental research on cold-bonded ceramsite based on the GP–fly ash–cement system, adopting the modified Andreasen–Andersen (MAA) particle packing model as a tool for mix ratio design and evaluation. By designing multiple groups of different particle size combinations, the raw material particle gradation is made to produce controllable deviations from the MAA target curve within a certain range. RSS is used to quantitatively characterize the degree of deviation of the particle gradation from the MAA target curve, and the influence mechanism of this deviation on the physical properties and pore structure of ceramsite is systematically analyzed. The results indicated that an RSS value of 6736 yielded the most compact ceramsite structure, which exhibited a cylinder compressive strength of 5.76 MPa, a bulk density of 1041 kg/m<sup>3</sup>, and a water absorption as low as 12.65 %. Further particle size fractionation experiments revealed that single-size raw material systems performed significantly worse than full-range particle distributions. The latter facilitated the formation of a skeleton–filler collaborative structure, thereby enhancing compactness and mechanical stability. Compared with existing utilization pathways of GP, the proposed structure-regulated preparation strategy for cold-bonded ceramsite enables up to 85 % incorporation of GP and delivers comprehensive performance improvement without reliance on high-temperature sintering or alkali activation. This approach demonstrates considerable engineering feasibility and application potential, providing a novel perspective and theoretical foundation for the high-efficiency valorization of low-activity solid wastes.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"109 ","pages":"Pages 86-98"},"PeriodicalIF":4.3,"publicationDate":"2025-12-09","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145838163","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-06DOI: 10.1016/j.partic.2025.11.019
Gansu Zhang , Tianxin Li , Hongyang Li , Zhiqiang Li , Shuxian Su , Xuan Xu , Wei Dai , Liang Dong
This study presents a comprehensive framework for the separation dynamic model of Air Dense Medium Fluidized Bed (ADMFB) to promote the intelligentization of coal preparation. The framework is a double-layer composite structure. In the outer layer, the static model of partition was extended from Dense Medium Cyclones to ADMFB. In the inner layer, the dynamic model of bed density was developed from the coupling model to the decoupling model with self-balancing characteristics. The model predicts product yield and ash content, which is validated against industrial separation data. The baseline performance is good but unstable, with maximum relative error 38.43 % and minimum relative error 4.48 % for coal ash content. To address this, an ash correction algorithm was innovatively put forward by introducing organic efficiency θ. The performance improvement is significant that coal ash content has maximum relative error 5.97 % and minimum relative error 0.48 %. Finally, Model Predictive Control (MPC) was implemented following the global linearization of the nonlinear bed density model, whose convergence speed to reach the tracking value is 46 % faster than constant control. Overall, this work provides a pathway for coal preparation plants to achieve more stable and intelligent production.
{"title":"Separation dynamic model of air dense medium fluidized bed for coal beneficiation and control","authors":"Gansu Zhang , Tianxin Li , Hongyang Li , Zhiqiang Li , Shuxian Su , Xuan Xu , Wei Dai , Liang Dong","doi":"10.1016/j.partic.2025.11.019","DOIUrl":"10.1016/j.partic.2025.11.019","url":null,"abstract":"<div><div>This study presents a comprehensive framework for the separation dynamic model of Air Dense Medium Fluidized Bed (ADMFB) to promote the intelligentization of coal preparation. The framework is a double-layer composite structure. In the outer layer, the static model of partition was extended from Dense Medium Cyclones to ADMFB. In the inner layer, the dynamic model of bed density was developed from the coupling model to the decoupling model with self-balancing characteristics. The model predicts product yield and ash content, which is validated against industrial separation data. The baseline performance is good but unstable, with maximum relative error 38.43 % and minimum relative error 4.48 % for coal ash content. To address this, an ash correction algorithm was innovatively put forward by introducing organic efficiency <em>θ</em>. The performance improvement is significant that coal ash content has maximum relative error 5.97 % and minimum relative error 0.48 %. Finally, Model Predictive Control (MPC) was implemented following the global linearization of the nonlinear bed density model, whose convergence speed to reach the tracking value is 46 % faster than constant control. Overall, this work provides a pathway for coal preparation plants to achieve more stable and intelligent production.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"108 ","pages":"Pages 320-335"},"PeriodicalIF":4.3,"publicationDate":"2025-12-06","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145787556","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-05DOI: 10.1016/j.partic.2025.12.001
Junhai Deng , Jiuhua Chen , Shuyao Feng , Yunyun Tian , Yingqi Liao , Bi Luo , Luchang Han , Yefeng Zhou
The stirred tank reactor is widely used for preparing Li-ion batteries precursors, and the high-performance materials are utilized in various fields such as electronic devices. However, controlling the particle characteristics remains a significant challenge due to the complex interaction between fluid dynamics and crystallization kinetics. Therefore, this work proposes the computational fluid dynamics-population balance model coupled model to simulate Ni(OH)2 reactive crystallization. By altering the structure and operation, this work analyzes effects of turbulence parameters on particle characteristics. Results show that increasing the height, baffle number and rotational speed enhances turbulence parameters, which reduces the Sauter mean diameter about 1.08–2.14 times and decreases the span from 1.6 to 1.17. Axial-flow impellers generate lower turbulent dissipation and shear force compared to radial-flow impellers, causing less particle breakage and better suitability for reactive crystallization. The wave bottom enhances turbulent dissipation about 1.19–1.38 times compared to flat and round bottom, improving flow circulation and reducing dead zones. Moreover, experiment and simulation demonstrate consistent trend in particle size and distribution under different baffle numbers, with morphology becoming better. This work provides important theoretical support for optimizing reactor design and enhancing reactive crystallization, facilitating the production of high-performance materials.
{"title":"Numerical investigation on reactive crystallization of Li-ion batteries precursor Ni(OH)2 in a stirred tank: Effect of structural factors on particle size and distribution","authors":"Junhai Deng , Jiuhua Chen , Shuyao Feng , Yunyun Tian , Yingqi Liao , Bi Luo , Luchang Han , Yefeng Zhou","doi":"10.1016/j.partic.2025.12.001","DOIUrl":"10.1016/j.partic.2025.12.001","url":null,"abstract":"<div><div>The stirred tank reactor is widely used for preparing Li-ion batteries precursors, and the high-performance materials are utilized in various fields such as electronic devices. However, controlling the particle characteristics remains a significant challenge due to the complex interaction between fluid dynamics and crystallization kinetics. Therefore, this work proposes the computational fluid dynamics-population balance model coupled model to simulate Ni(OH)<sub>2</sub> reactive crystallization. By altering the structure and operation, this work analyzes effects of turbulence parameters on particle characteristics. Results show that increasing the height, baffle number and rotational speed enhances turbulence parameters, which reduces the Sauter mean diameter about 1.08–2.14 times and decreases the span from 1.6 to 1.17. Axial-flow impellers generate lower turbulent dissipation and shear force compared to radial-flow impellers, causing less particle breakage and better suitability for reactive crystallization. The wave bottom enhances turbulent dissipation about 1.19–1.38 times compared to flat and round bottom, improving flow circulation and reducing dead zones. Moreover, experiment and simulation demonstrate consistent trend in particle size and distribution under different baffle numbers, with morphology becoming better. This work provides important theoretical support for optimizing reactor design and enhancing reactive crystallization, facilitating the production of high-performance materials.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"108 ","pages":"Pages 307-319"},"PeriodicalIF":4.3,"publicationDate":"2025-12-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145735087","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Industrial processes based on packed beds with gaseous flow come with high energy and resource consumption. To gain a better understanding of these phenomena, it is essential to investigate flow properties inside such systems. This study presents a novel reactor concept that allows for direct optical measurements inside the voids of the packing. It is based on polyhedral parallel arranged particles in a modular way. Through the modularity different regular and irregular configurations can be generated allowing for direct optical access avoiding major distortion. Particle Image Velocimetry (PIV) is applied to obtain spatially and temporally highly resolved 2D flow fields of the ambient temperature gas flow through the packing. Two different particle Reynolds numbers (100 and 1000) are investigated to validate the concept of the novel reactor model. The successful application of PIV to the inner pores of the bed, delivering reliable snapshot based data, mean velocity and turbulent kinetic energy of the gas flow, shows the potential of this reactor concept also for other optical measurement techniques that allow for the validation of numerical models and simulations of packed bed reactors.
{"title":"Allowing optical measurements in a 3D packed bed with gas flow: A novel reactor concept","authors":"Christin Velten, Kerstin Hülz, Katharina Zähringer","doi":"10.1016/j.partic.2025.11.018","DOIUrl":"10.1016/j.partic.2025.11.018","url":null,"abstract":"<div><div>Industrial processes based on packed beds with gaseous flow come with high energy and resource consumption. To gain a better understanding of these phenomena, it is essential to investigate flow properties inside such systems. This study presents a novel reactor concept that allows for direct optical measurements inside the voids of the packing. It is based on polyhedral parallel arranged particles in a modular way. Through the modularity different regular and irregular configurations can be generated allowing for direct optical access avoiding major distortion. Particle Image Velocimetry (PIV) is applied to obtain spatially and temporally highly resolved 2D flow fields of the ambient temperature gas flow through the packing. Two different particle Reynolds numbers (100 and 1000) are investigated to validate the concept of the novel reactor model. The successful application of PIV to the inner pores of the bed, delivering reliable snapshot based data, mean velocity and turbulent kinetic energy of the gas flow, shows the potential of this reactor concept also for other optical measurement techniques that allow for the validation of numerical models and simulations of packed bed reactors.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"108 ","pages":"Pages 293-306"},"PeriodicalIF":4.3,"publicationDate":"2025-12-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145735086","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-04DOI: 10.1016/j.partic.2025.11.017
Bin Li, Lele Yang, Xiaodong Chen, Chengyu Huang, Yue Wu
In this study, a coupled CFD–DEM framework incorporating heat transfer was established to elucidate the transport and deposition behavior of proppant particles in supercritical CO2 (SC-CO2) fracturing. A three-dimensional fracture-scale physical model was developed to investigate the effects of particle concentration, density, diameter, and non-sphericity on the evolution of the proppant bed. The simulations reveal that both the equilibrium height and length of the granular bed increase with particle concentration, exhibiting a near-linear dependence on the injected mass flux. As particle density rises, the bed height increases while the deposition front advances upstream, facilitating earlier bed formation. Increasing particle diameter from 0.4 mm to 1 mm produces pronounced morphological changes—larger particles form thicker, shorter beds, whereas smaller particles are more easily transported to distal fracture regions. Enhanced particle non-sphericity promotes the development of higher and wider beds due to increased mechanical interlocking and larger inter-particle voids, which strengthen flow-channel connectivity and potentially improve hydrocarbon recovery. The integrated thermal–hydrodynamic–granular analysis demonstrates that SC-CO2's temperature-dependent viscosity and density variations significantly modulate drag, lift, and buoyancy forces, jointly governing the self-organization and stability of proppant beds within fractures.
{"title":"Evaluation of effects of particle parameters on the particle bed in supercritical CO2 fractures using coupled CFD-DEM approach","authors":"Bin Li, Lele Yang, Xiaodong Chen, Chengyu Huang, Yue Wu","doi":"10.1016/j.partic.2025.11.017","DOIUrl":"10.1016/j.partic.2025.11.017","url":null,"abstract":"<div><div>In this study, a coupled CFD–DEM framework incorporating heat transfer was established to elucidate the transport and deposition behavior of proppant particles in supercritical CO<sub>2</sub> (SC-CO<sub>2</sub>) fracturing. A three-dimensional fracture-scale physical model was developed to investigate the effects of particle concentration, density, diameter, and non-sphericity on the evolution of the proppant bed. The simulations reveal that both the equilibrium height and length of the granular bed increase with particle concentration, exhibiting a near-linear dependence on the injected mass flux. As particle density rises, the bed height increases while the deposition front advances upstream, facilitating earlier bed formation. Increasing particle diameter from 0.4 mm to 1 mm produces pronounced morphological changes—larger particles form thicker, shorter beds, whereas smaller particles are more easily transported to distal fracture regions. Enhanced particle non-sphericity promotes the development of higher and wider beds due to increased mechanical interlocking and larger inter-particle voids, which strengthen flow-channel connectivity and potentially improve hydrocarbon recovery. The integrated thermal–hydrodynamic–granular analysis demonstrates that SC-CO<sub>2</sub>'s temperature-dependent viscosity and density variations significantly modulate drag, lift, and buoyancy forces, jointly governing the self-organization and stability of proppant beds within fractures.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"109 ","pages":"Pages 12-24"},"PeriodicalIF":4.3,"publicationDate":"2025-12-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145789278","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-12-01DOI: 10.1016/j.partic.2025.10.013
Martin Olazar , Gartzen Lopez , Xiaotao Bi , Xiaojun Bao , Choon Jim Lim
{"title":"Preface to special issue: Advances in spouted beds – The 8th International Symposium on Spouted Beds in honour of Norman Epstein","authors":"Martin Olazar , Gartzen Lopez , Xiaotao Bi , Xiaojun Bao , Choon Jim Lim","doi":"10.1016/j.partic.2025.10.013","DOIUrl":"10.1016/j.partic.2025.10.013","url":null,"abstract":"","PeriodicalId":401,"journal":{"name":"Particuology","volume":"107 ","pages":"Pages 375-376"},"PeriodicalIF":4.3,"publicationDate":"2025-12-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145748250","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-11-29DOI: 10.1016/j.partic.2025.11.013
Han Pu, Jiliang Ma, Jialiang Cai, Yi Wang, Xiaoping Chen, Cai Liang, Daoyin Liu, Meng Liu
The phenomenon of particle agglomeration in a liquid-containing fluidized bed is closely associated with the interactions between gas and solid phases, as well as the evaporation of the liquid component. This study performs an experimental investigation to examine the interactions among particle growth, fluidization behavior, and droplet evaporation within a continuous top-spray fluidized bed system. The research indicates that increased drying air temperatures generate severe drying conditions that promote the conversion of liquid bridges to solid bridges between particles. This conversion significantly decreases the nucleation time and encourages a more consistent distribution of agglomerate sizes. Additionally, a rise in the spraying rate and binder viscosity, strengthen the cohesive forces among particles, resulting in the development of larger agglomerates. The evaporation of the liquid binder exhibits a substantial correlation with the behavior of bubbles within the bed, which in turn affects particle growth and the chaotic dynamics of the fluidized bed system. The process of particle growth is delineated into two separate phases: nucleation growth and shell growth. Notably, the duration of nucleation growth phase exceeds that of the shell growth phase. Ultimately, a regime map has been developed to evaluate the feasibility of the spray granulation process concerning fluidization and drying parameters. The findings suggest that excessively low fluidization numbers, coupled with inadequate drying conditions, could lead to the failure of the liquid-containing fluidization process.
{"title":"Influence of fluidization dynamics and liquid evaporation on particle growth in a top-spray fluidized bed","authors":"Han Pu, Jiliang Ma, Jialiang Cai, Yi Wang, Xiaoping Chen, Cai Liang, Daoyin Liu, Meng Liu","doi":"10.1016/j.partic.2025.11.013","DOIUrl":"10.1016/j.partic.2025.11.013","url":null,"abstract":"<div><div>The phenomenon of particle agglomeration in a liquid-containing fluidized bed is closely associated with the interactions between gas and solid phases, as well as the evaporation of the liquid component. This study performs an experimental investigation to examine the interactions among particle growth, fluidization behavior, and droplet evaporation within a continuous top-spray fluidized bed system. The research indicates that increased drying air temperatures generate severe drying conditions that promote the conversion of liquid bridges to solid bridges between particles. This conversion significantly decreases the nucleation time and encourages a more consistent distribution of agglomerate sizes. Additionally, a rise in the spraying rate and binder viscosity, strengthen the cohesive forces among particles, resulting in the development of larger agglomerates. The evaporation of the liquid binder exhibits a substantial correlation with the behavior of bubbles within the bed, which in turn affects particle growth and the chaotic dynamics of the fluidized bed system. The process of particle growth is delineated into two separate phases: nucleation growth and shell growth. Notably, the duration of nucleation growth phase exceeds that of the shell growth phase. Ultimately, a regime map has been developed to evaluate the feasibility of the spray granulation process concerning fluidization and drying parameters. The findings suggest that excessively low fluidization numbers, coupled with inadequate drying conditions, could lead to the failure of the liquid-containing fluidization process.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"108 ","pages":"Pages 280-292"},"PeriodicalIF":4.3,"publicationDate":"2025-11-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145683488","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2025-11-28DOI: 10.1016/j.partic.2025.11.016
Ziru Wang , Li Gao , Ying Zhang , Xia Zhang , Bingsen Zhang
ZSM-5 zeolite has emerged as an outstanding catalyst in converting waste plastics into high-value chemicals. Constructing hierarchical micro-mesoporous ZSM-5 can significantly enhance diffusion characteristics and consequently improve catalytic cracking performance. The morphology of ZSM-5 plays a crucial role in altering its catalytic hydrocracking efficiency in plastic degradation, but the reasons behind this is not clear. Herein, by precisely adjusting the structure-directing agent (SDA) ratio to control nucleation dynamics, we have developed a morphology-controlled synthesis strategy for ZSM-5 zeolites. Two distinct hierarchical ZSM-5 catalysts were successfully fabricated: plate-shaped n-ZSM-5 and quasi-spherical s-ZSM-5. And, increasing the SDA content was worked in promoting nucleation kinetics, facilitating the incorporation of active components into the zeolite framework, and increasing surface acid site density. The plate-shaped n-ZSM-5 exhibited exceptional catalytic performance in polypropylene hydrocracking with a liquid yield of 57.3 %, and proved to maintain effective activity for the actual conversion of plastic waste. The catalytic mechanism reveals that the morphology engineering can effectively regulate mass transport within catalyst pores, provide a novel approach for tailoring zeolite catalyst properties. This work offers fundamental insights into structure-performance relationships for advanced plastic upcycling catalysts.
{"title":"Morphology controlled synthesis of ZSM-5 and enhanced catalytic activity in polypropylene hydrocracking","authors":"Ziru Wang , Li Gao , Ying Zhang , Xia Zhang , Bingsen Zhang","doi":"10.1016/j.partic.2025.11.016","DOIUrl":"10.1016/j.partic.2025.11.016","url":null,"abstract":"<div><div>ZSM-5 zeolite has emerged as an outstanding catalyst in converting waste plastics into high-value chemicals. Constructing hierarchical micro-mesoporous ZSM-5 can significantly enhance diffusion characteristics and consequently improve catalytic cracking performance. The morphology of ZSM-5 plays a crucial role in altering its catalytic hydrocracking efficiency in plastic degradation, but the reasons behind this is not clear. Herein, by precisely adjusting the structure-directing agent (SDA) ratio to control nucleation dynamics, we have developed a morphology-controlled synthesis strategy for ZSM-5 zeolites. Two distinct hierarchical ZSM-5 catalysts were successfully fabricated: plate-shaped n-ZSM-5 and quasi-spherical s-ZSM-5. And, increasing the SDA content was worked in promoting nucleation kinetics, facilitating the incorporation of active components into the zeolite framework, and increasing surface acid site density. The plate-shaped n-ZSM-5 exhibited exceptional catalytic performance in polypropylene hydrocracking with a liquid yield of 57.3 %, and proved to maintain effective activity for the actual conversion of plastic waste. The catalytic mechanism reveals that the morphology engineering can effectively regulate mass transport within catalyst pores, provide a novel approach for tailoring zeolite catalyst properties. This work offers fundamental insights into structure-performance relationships for advanced plastic upcycling catalysts.</div></div>","PeriodicalId":401,"journal":{"name":"Particuology","volume":"108 ","pages":"Pages 272-279"},"PeriodicalIF":4.3,"publicationDate":"2025-11-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145683487","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}