The hydrophobicity and floatability of fine coal slime are severely diminished by surface coatings of gangue minerals, complicating coal–gangue separation in slurry systems. Traditional pulping methods struggle to efficiently remove fine mud from coal particles, reducing recovery efficiency. To address this, a self-designed impact flow slurry conditioning device was developed to enhance reagent adsorption on coal surfaces. Combining computational fluid dynamics (CFD) simulations, reagent adsorption rate analysis, and contact angle measurements, this study optimized slurry impact velocity to evaluate flow field dynamics and conditioning mechanisms. Flotation experiments revealed that strain rate increased with impact velocity, peaking at 774 s−1 (5 m/s), while the minimum vortex scale reached 1.04 μm at 4 m/s. At 4 m/s, the collector adsorption rate and coal contact angle were maximized, achieving a combustible recovery rate of 98.18%, indicating optimal flotation performance. The impact flow method effectively strips surface gangue coatings, enhances coal-gangue separation, and improves coal hydrophobicity and floatability. The device integrates a disturbing cone and plate to generate localized turbulence and shear fields, significantly boosting reagent adsorption efficiency and overcoming structural limitations of traditional stirring equipment. These innovations provide critical insights into shear-driven adsorption mechanisms and advance coal slurry flotation technology, offering a scalable solution for industrial applications. This research establishes a foundation for developing efficient, high-performance coal processing systems.
{"title":"Study on the analysis of flow field and enhancing the fine coal flotation by the impingement flow","authors":"Youli Han, Zhiyong Lin, Qinghui Shi, Shuwei Xia, Zhiqian Qin, Jinbo Zhu, Fanfei Min","doi":"10.1002/cjce.70047","DOIUrl":"https://doi.org/10.1002/cjce.70047","url":null,"abstract":"<p>The hydrophobicity and floatability of fine coal slime are severely diminished by surface coatings of gangue minerals, complicating coal–gangue separation in slurry systems. Traditional pulping methods struggle to efficiently remove fine mud from coal particles, reducing recovery efficiency. To address this, a self-designed impact flow slurry conditioning device was developed to enhance reagent adsorption on coal surfaces. Combining computational fluid dynamics (CFD) simulations, reagent adsorption rate analysis, and contact angle measurements, this study optimized slurry impact velocity to evaluate flow field dynamics and conditioning mechanisms. Flotation experiments revealed that strain rate increased with impact velocity, peaking at 774 s<sup>−1</sup> (5 m/s), while the minimum vortex scale reached 1.04 μm at 4 m/s. At 4 m/s, the collector adsorption rate and coal contact angle were maximized, achieving a combustible recovery rate of 98.18%, indicating optimal flotation performance. The impact flow method effectively strips surface gangue coatings, enhances coal-gangue separation, and improves coal hydrophobicity and floatability. The device integrates a disturbing cone and plate to generate localized turbulence and shear fields, significantly boosting reagent adsorption efficiency and overcoming structural limitations of traditional stirring equipment. These innovations provide critical insights into shear-driven adsorption mechanisms and advance coal slurry flotation technology, offering a scalable solution for industrial applications. This research establishes a foundation for developing efficient, high-performance coal processing systems.</p>","PeriodicalId":9400,"journal":{"name":"Canadian Journal of Chemical Engineering","volume":"104 2","pages":"1039-1050"},"PeriodicalIF":1.9,"publicationDate":"2025-08-03","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145904751","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
{"title":"Issue Highlights","authors":"","doi":"10.1002/cjce.25335","DOIUrl":"https://doi.org/10.1002/cjce.25335","url":null,"abstract":"","PeriodicalId":9400,"journal":{"name":"Canadian Journal of Chemical Engineering","volume":"103 9","pages":""},"PeriodicalIF":1.9,"publicationDate":"2025-08-03","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"144767441","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Luis Antonio Velázquez Herrera, José Ángel Cobos Murcia, Leticia López Zamora
The present research provides a thorough investigation to enhance the delignification process in a 2G biorefinery by implementing a dynamic process simulator. Developed using the Julia programming language, this simulator enables the study of crucial variables such as liquid–solid ratio (LSR), hydrogen peroxide concentration (CHP), and processing time (t) during the alkaline hydrolysis stage. Optimal operating conditions were determined through rigorous simulation and meticulous experimental validation, resulting in an optimal configuration of 4% H2O2 concentration, LSR of 15:1 v/w, and 50 h of processing time under standard pressure and temperature conditions. These findings yielded a lignin removal percentage of 93.02%. Furthermore, the experimental validation process facilitated the recalibration of kinetic parameters. Overall, this research underscores the potential of the dynamic simulator in optimizing critical variables across various raw materials.
{"title":"Modelling and simulation of the sugarcane delignification process by alkaline pretreatment using H2O2","authors":"Luis Antonio Velázquez Herrera, José Ángel Cobos Murcia, Leticia López Zamora","doi":"10.1002/cjce.70055","DOIUrl":"https://doi.org/10.1002/cjce.70055","url":null,"abstract":"<p>The present research provides a thorough investigation to enhance the delignification process in a 2G biorefinery by implementing a dynamic process simulator. Developed using the Julia programming language, this simulator enables the study of crucial variables such as liquid–solid ratio (LSR), hydrogen peroxide concentration (<i>C</i><sub>HP</sub>), and processing time (<i>t</i>) during the alkaline hydrolysis stage. Optimal operating conditions were determined through rigorous simulation and meticulous experimental validation, resulting in an optimal configuration of 4% H<sub>2</sub>O<sub>2</sub> concentration, LSR of 15:1 v/w, and 50 h of processing time under standard pressure and temperature conditions. These findings yielded a lignin removal percentage of 93.02%. Furthermore, the experimental validation process facilitated the recalibration of kinetic parameters. Overall, this research underscores the potential of the dynamic simulator in optimizing critical variables across various raw materials.</p>","PeriodicalId":9400,"journal":{"name":"Canadian Journal of Chemical Engineering","volume":"104 3","pages":"1211-1222"},"PeriodicalIF":1.9,"publicationDate":"2025-07-31","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"146154904","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Aiming at the problems of layer information loss as well as the effectiveness of process data spatio-temporal feature fusion in stacked network-based soft sensor methods, this paper proposes a dual-attention spatio-temporal interaction network (DA-TSINET) method. Firstly, the dual-attention stacked network is constructed to overcome the layer information loss. Self-attention is added to different layers of stacked denoising autoencoder (SDAE) to enhance local denoising features, and global enhanced features are obtained by self-attention fusion. A gated recurrent unit (GRU) and a convolutional neural network (CNN) are used in parallel to further extract spatio-temporal relations, and an interactive gating module is designed for fusion to obtain globally enhanced spatio-temporal features for constructing a soft sensor model. Simulation experiments are carried out by debutanizer column and thermal power plant and compared with stacked autoencoder (SAE), SDAE, stacked isomorphic autoencoder (SIAE), variable-wise weighted SAE (VW-SAE), and gated stacked target-related autoencoder (GSTAE); the results show that the proposed method has high prediction accuracy, which verifies the effectiveness of the proposed method.
{"title":"Soft sensor of processes based on dual attention spatio-temporal interaction network","authors":"Xiaoping Guo, Lingling Yu, Yuan Li","doi":"10.1002/cjce.70045","DOIUrl":"https://doi.org/10.1002/cjce.70045","url":null,"abstract":"<p>Aiming at the problems of layer information loss as well as the effectiveness of process data spatio-temporal feature fusion in stacked network-based soft sensor methods, this paper proposes a dual-attention spatio-temporal interaction network (DA-TSINET) method. Firstly, the dual-attention stacked network is constructed to overcome the layer information loss. Self-attention is added to different layers of stacked denoising autoencoder (SDAE) to enhance local denoising features, and global enhanced features are obtained by self-attention fusion. A gated recurrent unit (GRU) and a convolutional neural network (CNN) are used in parallel to further extract spatio-temporal relations, and an interactive gating module is designed for fusion to obtain globally enhanced spatio-temporal features for constructing a soft sensor model. Simulation experiments are carried out by debutanizer column and thermal power plant and compared with stacked autoencoder (SAE), SDAE, stacked isomorphic autoencoder (SIAE), variable-wise weighted SAE (VW-SAE), and gated stacked target-related autoencoder (GSTAE); the results show that the proposed method has high prediction accuracy, which verifies the effectiveness of the proposed method.</p>","PeriodicalId":9400,"journal":{"name":"Canadian Journal of Chemical Engineering","volume":"104 2","pages":"847-863"},"PeriodicalIF":1.9,"publicationDate":"2025-07-31","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"145905240","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Luis Antonio Velázquez Herrera, José Ángel Cobos Murcia, Leticia López Zamora
The present research provides a thorough investigation to enhance the delignification process in a 2G biorefinery by implementing a dynamic process simulator. Developed using the Julia programming language, this simulator enables the study of crucial variables such as liquid–solid ratio (LSR), hydrogen peroxide concentration (CHP), and processing time (t) during the alkaline hydrolysis stage. Optimal operating conditions were determined through rigorous simulation and meticulous experimental validation, resulting in an optimal configuration of 4% H2O2 concentration, LSR of 15:1 v/w, and 50 h of processing time under standard pressure and temperature conditions. These findings yielded a lignin removal percentage of 93.02%. Furthermore, the experimental validation process facilitated the recalibration of kinetic parameters. Overall, this research underscores the potential of the dynamic simulator in optimizing critical variables across various raw materials.
{"title":"Modelling and simulation of the sugarcane delignification process by alkaline pretreatment using H2O2","authors":"Luis Antonio Velázquez Herrera, José Ángel Cobos Murcia, Leticia López Zamora","doi":"10.1002/cjce.70055","DOIUrl":"https://doi.org/10.1002/cjce.70055","url":null,"abstract":"<p>The present research provides a thorough investigation to enhance the delignification process in a 2G biorefinery by implementing a dynamic process simulator. Developed using the Julia programming language, this simulator enables the study of crucial variables such as liquid–solid ratio (LSR), hydrogen peroxide concentration (<i>C</i><sub>HP</sub>), and processing time (<i>t</i>) during the alkaline hydrolysis stage. Optimal operating conditions were determined through rigorous simulation and meticulous experimental validation, resulting in an optimal configuration of 4% H<sub>2</sub>O<sub>2</sub> concentration, LSR of 15:1 v/w, and 50 h of processing time under standard pressure and temperature conditions. These findings yielded a lignin removal percentage of 93.02%. Furthermore, the experimental validation process facilitated the recalibration of kinetic parameters. Overall, this research underscores the potential of the dynamic simulator in optimizing critical variables across various raw materials.</p>","PeriodicalId":9400,"journal":{"name":"Canadian Journal of Chemical Engineering","volume":"104 3","pages":"1211-1222"},"PeriodicalIF":1.9,"publicationDate":"2025-07-31","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"146154887","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
This study presents a three-dimensional computational analysis of inertial flow behaviour, hydraulic resistance, and thermodynamic performance in asymmetrical converging–diverging microchannels. Three configurations are examined by introducing asymmetries in the lower arm—through variations in tapering angle, throat width, and throat length—while keeping the upper arm unchanged. Flow distribution analysis reveals that the steep-angle design achieves the most balanced flow split, improving symmetry by approximately 55% and 83% compared to the extended-throat and wide-throat designs, respectively. At a representative flow rate of 20 μL/min, the wide-throat configuration exhibits the lowest flow resistance, reducing pressure drop by 46.7% and 28.0% relative to the extended-throat and steep-angle cases, respectively. The steep-angle design also outperforms the extended-throat geometry by 26.0%. In terms of thermodynamic performance, entropy generation is lowest in the steep-angle configuration, showing a 27% reduction compared to the extended-throat case for Re