The flotation separation of pyrite (Py) from serpentine (Spt) was studied using xanthamonas campestris (XC) as a novel Spt depressant. The adsorption of XC onto Spt and Py was observed to decrease with increase in pH attesting to increased repulsion between the negatively charged carboxylate portion of XC and the increased negativity of the mineral surface. However, the polysaccharide adsorption onto Py was less than that onto Spt due to a higher iso-electric point (IEP) of Spt compared to that of Py. Further, theoretical investigations using quantum theory of atoms in molecules (QTAIM) revealed that XC adsorption onto Spt was due to hydrogen bonding (HB), partial and non-covalent interactions, whereas that onto Py was due to partial covalent and non-covalent interactions. Additionally and in general, the adsorption of XC onto the minerals was due to the shift of electrons from the polysaccharide to mineral surface species. Flotation studies conducted at pH 7.8 of Py-Spt (1:1) in presence of 20 g/t, 80 g/t and 60 g/t of sodium tripolyphosphate (SPP), XC and potassium amyl xanthate (PAX) yielded Py grade and separation efficiency of 98.7 % and 97.8 %, respectively, at an economical cost. Therefore, XC is a potential depressant for Spt.
{"title":"New insights into the surface chemical properties of serpentine and flotation of pyrite using xanthomonas campestris as a novel selective serpentine depressant: Experimental and DFT investigation","authors":"Levie Mweene , Govinda Prasad Khanal , Emmanuel Etim","doi":"10.1016/j.mineng.2024.109141","DOIUrl":"10.1016/j.mineng.2024.109141","url":null,"abstract":"<div><div>The flotation separation of pyrite (Py) from serpentine (Spt) was studied using xanthamonas campestris (XC) as a novel Spt depressant. The adsorption of XC onto Spt and Py was observed to decrease with increase in pH attesting to increased repulsion between the negatively charged carboxylate portion of XC and the increased negativity of the mineral surface. However, the polysaccharide adsorption onto Py was less than that onto Spt due to a higher <em>iso</em>-electric point (IEP) of Spt compared to that of Py. Further, theoretical investigations using quantum theory of atoms in molecules (QTAIM) revealed that XC adsorption onto Spt was due to hydrogen bonding (HB), partial and non-covalent interactions, whereas that onto Py was due to partial covalent and non-covalent interactions. Additionally and in general, the adsorption of XC onto the minerals was due to the shift of electrons from the polysaccharide to mineral surface species. Flotation studies conducted at pH 7.8 of Py-Spt (1:1) in presence of 20 g/t, 80 g/t and 60 g/t of sodium tripolyphosphate (SPP), XC and potassium amyl xanthate (PAX) yielded Py grade and separation efficiency of 98.7 % and 97.8 %, respectively, at an economical cost. Therefore, XC is a potential depressant for Spt.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109141"},"PeriodicalIF":4.9,"publicationDate":"2024-12-05","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142790162","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-12-03DOI: 10.1016/j.mineng.2024.109129
Saeed Abdollahi , Sajjad Afraei , Akbar Mehdilo , Reza Kouchakzadeh , Mehdi Irannajad
Flotation is the most essential method for the concentration of phosphate reserves and, hence, the production of apatite concentrate. With the reduction of high-grade reserves and the necessity of exploiting low-grade phosphate ores, many efforts have been made to use different chemical reagents alone and their combinations as collectors for apatite flotation and achieving high-quality concentrates for preparing phosphoric acid and fertilizers. This work focuses on applying direct apatite flotation by employing a novel mixture of fatty acid collectors to optimize the apatite processing plants. Extensive experiments using tall oil fatty acid (TOFA) and oleic acid polyethylene glycol ester 6 mol (OAPEGE6) alone and their mixture in different ratios were conducted in micro-flotation, bench flotation, and plant flotation scales. The micro-flotation experiments showed that using OAPEGE6 and TOFA, the flotation recovery of apatite at a pH of 9.5 is 46% and 86%, respectively. However, by mixing TOFA and OAPEGE6 in a weight ratio of 70% to 30%, the flotation recovery of apatite increases to 95%. At this weight ratio of TOFA and OAPEGE6 using a 600 mixed collector, an apatite concentrate containing 23.2% with a recovery of 90.4% is achieved by rougher stage bench flotation in laboratory experiments. Finally, using the mixed collector with the formulation mentioned above on a plant-scale, an apatite concentrate with almost 33% and 59% recovery is obtained through rougher and cleaner stages of the flotation process. FTIR analysis and zeta potential measurements show that the simultaneous presence of TOFA and OAPEGE6 with a synergetic effect can strengthen the chemisorption of oleate active species on the apatite surface. As confirmed by contact angle measurements, this improved the formation of an insoluble hydrophobic layer on the apatite surface and resulted in its flotation recovery.
{"title":"A new mixture of anionic collectors for improvement of apatite floatability","authors":"Saeed Abdollahi , Sajjad Afraei , Akbar Mehdilo , Reza Kouchakzadeh , Mehdi Irannajad","doi":"10.1016/j.mineng.2024.109129","DOIUrl":"10.1016/j.mineng.2024.109129","url":null,"abstract":"<div><div>Flotation is the most essential method for the concentration of phosphate reserves and, hence, the production of apatite concentrate. With the reduction of high-grade reserves and the necessity of exploiting low-grade phosphate ores, many efforts have been made to use different chemical reagents alone and their combinations as collectors for apatite flotation and achieving high-quality concentrates for preparing phosphoric acid and fertilizers. This work focuses on applying direct apatite flotation by employing a novel mixture of fatty acid collectors to optimize the apatite processing plants. Extensive experiments using tall oil fatty acid (TOFA) and oleic acid polyethylene glycol ester 6 mol (OAPEGE6) alone and their mixture in different ratios were conducted in micro-flotation, bench flotation, and plant flotation scales. The micro-flotation experiments showed that using OAPEGE6 and TOFA, the flotation recovery of apatite at a pH of 9.5 is 46% and 86%, respectively. However, by mixing TOFA and OAPEGE6 in a weight ratio of 70% to 30%, the flotation recovery of apatite increases to 95%. At this weight ratio of TOFA and OAPEGE6 using a 600 <span><math><mrow><mi>g</mi><mo>/</mo><mi>t</mi></mrow></math></span> mixed collector, an apatite concentrate containing 23.2% <span><math><mrow><msub><mrow><mi>P</mi></mrow><mrow><mn>2</mn></mrow></msub><msub><mrow><mi>O</mi></mrow><mrow><mn>5</mn></mrow></msub></mrow></math></span> with a recovery of 90.4% is achieved by rougher stage bench flotation in laboratory experiments. Finally, using the mixed collector with the formulation mentioned above on a plant-scale, an apatite concentrate with almost 33% <span><math><mrow><msub><mrow><mi>P</mi></mrow><mrow><mn>2</mn></mrow></msub><msub><mrow><mi>O</mi></mrow><mrow><mn>5</mn></mrow></msub></mrow></math></span> and 59% recovery is obtained through rougher and cleaner stages of the flotation process. FTIR analysis and zeta potential measurements show that the simultaneous presence of TOFA and OAPEGE6 with a synergetic effect can strengthen the chemisorption of oleate active species on the apatite surface. As confirmed by contact angle measurements, this improved the formation of an insoluble hydrophobic layer on the apatite surface and resulted in its flotation recovery.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109129"},"PeriodicalIF":4.9,"publicationDate":"2024-12-03","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142790054","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-11-29DOI: 10.1016/j.mineng.2024.109132
Abdessamad Khalil , Yassine Ait-khouia , Hamza Beniddar , Mustapha El Ghorfi , Rachid Hakkou , Yassine Taha , Mostafa Benzaazoua
The abandoned Touissit-Bou Beker mining district has accumulated tens of millions of tons of tailings, stored without environmental safeguards. Due to the limited ore processing method, the tailings exhibit a significant zinc (2 wt%) and lead (0.3 wt%) content, mainly buried in carbonate minerals. These tailings pose environmental concerns but also offer economic opportunities. This study investigated the feasibility of decontaminating these tailings using froth flotation to produce a clean mineral byproduct. Composite samples were collected via reverse circulation (RC) drilling, and flotation conditions were optimized. Quantitative mineralogy and environmental behavior were assessed using quantitative evaluation of materials by scanning electron microscope (QEMSCAN®) and toxicity characteristic leaching procedure (TCLP), respectively. Under optimal conditions — potassium amyl xanthate (KAX) 350 g/t, CuSO4 1,250 g/t, Na2S 1,250 g/t, sodium hexametaphosphate (SH) 1,750 g/t, and pH 11—Zn and Pb recoveries reached up to 94 % and 71 %, respectively. Residual Pb–Zn remained partially locked within the non-sulfide gangue minerals or present as slime particles. TCLP results indicate minimal risk, suggesting reprocessing mine tailings in abandoned mine sites in Morocco could offer economic and environmental benefits. The current study is expected to serve as a reference for decision-makers when evaluating sustainable management options for mine tailings.
{"title":"Sustainable reprocessing of Pb–Zn mine tailings through froth flotation for resource recovery and environmental remediation in abandoned mining regions","authors":"Abdessamad Khalil , Yassine Ait-khouia , Hamza Beniddar , Mustapha El Ghorfi , Rachid Hakkou , Yassine Taha , Mostafa Benzaazoua","doi":"10.1016/j.mineng.2024.109132","DOIUrl":"10.1016/j.mineng.2024.109132","url":null,"abstract":"<div><div>The abandoned Touissit-Bou Beker mining district has accumulated tens of millions of tons of tailings, stored without environmental safeguards. Due to the limited ore processing method, the tailings exhibit a significant zinc (2 wt%) and lead (0.3 wt%) content, mainly buried in carbonate minerals. These tailings pose environmental concerns but also offer economic opportunities. This study investigated the feasibility of decontaminating these tailings using froth flotation to produce a clean mineral byproduct. Composite samples were collected via reverse circulation (RC) drilling, and flotation conditions were optimized. Quantitative mineralogy and environmental behavior were assessed using quantitative evaluation of materials by scanning electron microscope (QEMSCAN®) and toxicity characteristic leaching procedure (TCLP), respectively. Under optimal conditions — potassium amyl xanthate (KAX) 350 g/t, CuSO<sub>4</sub> 1,250 g/t, Na<sub>2</sub>S 1,250 g/t, sodium hexametaphosphate (SH) 1,750 g/t, and pH 11—Zn and Pb recoveries reached up to 94 % and 71 %, respectively. Residual Pb–Zn remained partially locked within the non-sulfide gangue minerals or present as slime particles. TCLP results indicate minimal risk, suggesting reprocessing mine tailings in abandoned mine sites in Morocco could offer economic and environmental benefits. The current study is expected to serve as a reference for decision-makers when evaluating sustainable management options for mine tailings.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109132"},"PeriodicalIF":4.9,"publicationDate":"2024-11-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142747410","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-11-29DOI: 10.1016/j.mineng.2024.109111
Dusan Ilic, Aleksej Lavrinec, Kevin P. Galvin
A simulation model of a dry, vibrated, fluidized medium (VFM) with sinkhole arrangement was developed and used to investigate the separation of relatively dense, coarse particles. The objective of the new model was to emulate a most unusual experimental result involving the sinkhole arrangement, separation densities much higher than the bulk density of the fluidized medium. The VFM was simulated using spherical sand particles in diameter, and density of 2500 kg/m3, while spherical coarse particles 2 to 4 mm in diameter, with density ranging from 2100 to 8400 kg/m3, were used as the density tracers. Coupled computational fluid dynamics (CFD)/discrete element method (DEM) was used to simulate interactions for up to 10 s duration. Remarkably, the model reproduced separation densities much higher than the bulk density of the suspension. Different combinations of frequency and amplitude of vibration, air flow velocity, and volume of VFM were used. The separation density was found to scale directly with the amplitude, and scale with the frequency to the 0.33 power. Vibration intensity correlated poorly with separation density. The critical condition governing the tendency of a particle to float or sink was examined in terms of the volume fraction and the density of the bed profile in the vicinity of the sinkhole. A pronounced reduction in the bed density is evident near the base of the VFM for particles that sink. The average solid volume fraction is observed to vary from 0.58 during initial settling, decreasing as the particles sink. Interestingly, re-circulation of the VFM is needed for a tracer particle to sink. Re-circulation is dependent on, and increases with, airflow as the bed expands up to a maximum beyond which it again reduces.
{"title":"Model investigation of a dry vibrated fluidized sinkhole system for separating coarse particles based on density","authors":"Dusan Ilic, Aleksej Lavrinec, Kevin P. Galvin","doi":"10.1016/j.mineng.2024.109111","DOIUrl":"10.1016/j.mineng.2024.109111","url":null,"abstract":"<div><div>A simulation model of a dry, vibrated, fluidized medium (VFM) with sinkhole arrangement was developed and used to investigate the separation of relatively dense, coarse particles. The objective of the new model was to emulate a most unusual experimental result involving the sinkhole arrangement, separation densities much higher than the bulk density of the fluidized medium. The VFM was simulated using spherical sand particles <span><math><mrow><mn>225</mn><mspace></mspace><mi>μ</mi><mi>m</mi></mrow></math></span> in diameter, and density of 2500 kg/m<sup>3</sup>, while spherical coarse particles 2 to 4 mm in diameter, with density ranging from 2100 to 8400 kg/m<sup>3</sup>, were used as the density tracers. Coupled computational fluid dynamics (CFD)/discrete element method (DEM) was used to simulate interactions for up to 10 s duration. Remarkably, the model reproduced separation densities much higher than the bulk density of the suspension. Different combinations of frequency and amplitude of vibration, air flow velocity, and volume of VFM were used. The separation density was found to scale directly with the amplitude, and scale with the frequency to the 0.33 power. Vibration intensity correlated poorly with separation density. The critical condition governing the tendency of a particle to float or sink was examined in terms of the volume fraction and the density of the bed profile in the vicinity of the sinkhole. A pronounced reduction in the bed density is evident near the base of the VFM for particles that sink. The average solid volume fraction is observed to vary from 0.58 during initial settling, decreasing as the particles sink. Interestingly, re-circulation of the VFM is needed for a tracer particle to sink. Re-circulation is dependent on, and increases with, airflow as the bed expands up to a maximum beyond which it again reduces.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109111"},"PeriodicalIF":4.9,"publicationDate":"2024-11-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142747414","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-11-29DOI: 10.1016/j.mineng.2024.109125
Darwin Michell Cheje Machaca, Thamyres Cardoso de Carvalho, Jorge Alberto Soares Tenório, Denise Crocce Romano Espinosa
This article presents a comprehensive analysis of the challenges and advancements in the extraction of niobium (Nb) and tantalum (Ta), focusing on global production and the growing demand for strategic and critical metals. The extraction of these metals from their primary and secondary resources is carried out through well-known metallurgical techniques, based on the use of hydrofluoric acid in the various production chains. However, the operational processes and their sustainable production are hindered due to the negative impacts produced during the process, resulting in a particular challenge for the extraction of these two metals. Therefore, pyrometallurgical and hydrometallurgical processes have been explored as emerging alternatives to the existing commercial processes. Thermal treatment processes in acidic and alkaline media have been shown to be capable of preparing PLS loaded with the metals of interest. On the other hand, leaching using mineral and organic acids is essential for the efficient recovery of Nb and Ta, highlighting their advantages and limitations. Additionally, the precipitation of acidic or basic liquors from hydrometallurgy is described to advance towards selective recovery stages. In this context, emphasis is placed on traditional and novel extractants according to their separation function, to ensure the high quality of the products through current technology.
{"title":"Advancements in the extraction of niobium and tantalum: Innovative strategies in hydrometallurgical processes","authors":"Darwin Michell Cheje Machaca, Thamyres Cardoso de Carvalho, Jorge Alberto Soares Tenório, Denise Crocce Romano Espinosa","doi":"10.1016/j.mineng.2024.109125","DOIUrl":"10.1016/j.mineng.2024.109125","url":null,"abstract":"<div><div>This article presents a comprehensive analysis of the challenges and advancements in the extraction of niobium (Nb) and tantalum (Ta), focusing on global production and the growing demand for strategic and critical metals. The extraction of these metals from their primary and secondary resources is carried out through well-known metallurgical techniques, based on the use of hydrofluoric acid in the various production chains. However, the operational processes and their sustainable production are hindered due to the negative impacts produced during the process, resulting in a particular challenge for the extraction of these two metals. Therefore, pyrometallurgical and hydrometallurgical processes have been explored as emerging alternatives to the existing commercial processes. Thermal treatment processes in acidic and alkaline media have been shown to be capable of preparing PLS loaded with the metals of interest. On the other hand, leaching using mineral and organic acids is essential for the efficient recovery of Nb and Ta, highlighting their advantages and limitations. Additionally, the precipitation of acidic or basic liquors from hydrometallurgy is described to advance towards selective recovery stages. In this context, emphasis is placed on traditional and novel extractants according to their separation function, to ensure the high quality of the products through current technology.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109125"},"PeriodicalIF":4.9,"publicationDate":"2024-11-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142747415","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-11-29DOI: 10.1016/j.mineng.2024.109114
J.B. Starrett, K.P. Galvin
A REFLUX™ Classifier was used to classify a silica feed (0–710 µm) based on particle size. Split Fluidisation was used to generate remarkably sharp separations involving solids throughputs of up to 92 t/m2/h. This work builds on the previous study by Starrett and Galvin (2023) but with a focus on coarser separations at higher throughputs. As the separation size increased, there was increasing misplacement of fine particles in excess of 75 µm into the coarse underflow stream. This problem was averted by halving the cross-sectional area of the lower section of the REFLUX™ Classifier. This change led to a doubling of the superficial fluid velocity in the lower section for a given set of flow rates, ensuring fine particles were unable to settle into the coarse underflow. In general, the separations performed in this study show complete closure of the partition curve at both the coarse and fine ends. It was also found that to deliver sharp separations it is essential to introduce sufficient water to the separator, per unit of solids transport to the overflow, especially for higher solids throughputs with coarser separations. Although the fluidisation rate can be used to control the separation size at finer separations (below 180 µm) and lower throughputs, ultimately the bias flux provides the basis for controlling the separation size at coarser sizes and higher throughputs.
{"title":"Application of inclined channels in the hydrodynamic classification of minerals by particle size – Extension to coarser separations","authors":"J.B. Starrett, K.P. Galvin","doi":"10.1016/j.mineng.2024.109114","DOIUrl":"10.1016/j.mineng.2024.109114","url":null,"abstract":"<div><div>A REFLUX™ Classifier was used to classify a silica feed (0–710 µm) based on particle size. Split Fluidisation was used to generate remarkably sharp separations involving solids throughputs of up to 92 t/m<sup>2</sup>/h. This work builds on the previous study by <span><span>Starrett and Galvin (2023)</span></span> but with a focus on coarser separations at higher throughputs. As the separation size increased, there was increasing misplacement of fine particles in excess of 75 µm into the coarse underflow stream. This problem was averted by halving the cross-sectional area of the lower section of the REFLUX™ Classifier. This change led to a doubling of the superficial fluid velocity in the lower section for a given set of flow rates, ensuring fine particles were unable to settle into the coarse underflow. In general, the separations performed in this study show complete closure of the partition curve at both the coarse and fine ends. It was also found that to deliver sharp separations it is essential to introduce sufficient water to the separator, per unit of solids transport to the overflow, especially for higher solids throughputs with coarser separations. Although the fluidisation rate can be used to control the separation size at finer separations (below 180 µm) and lower throughputs, ultimately the bias flux provides the basis for controlling the separation size at coarser sizes and higher throughputs.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109114"},"PeriodicalIF":4.9,"publicationDate":"2024-11-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142747411","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-11-29DOI: 10.1016/j.mineng.2024.109126
Mianyan Yang, Zhijun Zhang
The effect of surface roughness on the detachment between the bubbles and the glass beads (soda-lime) was comprehensively investigated. Glass beads with dimensions of −1.20 + 1.12 mm were acid etched to achieve varying degrees of surface roughness, followed by silanation reactions conducted for different immersion times. The characterization of surface roughness was conducted using a ContourGT-K 3D optical microscope. Measurements of receding contact angle, induction time and detachment force were conducted to assess the influence of surface roughness on bubble and glass bead attachment/detachment. It is observed that the etching surface of glass beads with uniform protrusions and depressions, the hydrophobic glass beads exhibited shorter induction time, larger contact angle and higher critical detachment force. However, the stability of aggregates of bubbles and hydrophilic glass beads was reduced, making them prone to detachment. Moreover, larger protrusions and depressions on hydrophobic glass bead surfaces with increasing etching time, resulted in an increase in induction time, a decrease in receding contact angle and critical detachment force. The stability of bubbles and hydrophilic glass bead aggregates remained unchanged.
{"title":"Exploring the influence of surface roughness on the interface phenomenon between an air bubble and a glass bead: An experimental and theoretical investigation","authors":"Mianyan Yang, Zhijun Zhang","doi":"10.1016/j.mineng.2024.109126","DOIUrl":"10.1016/j.mineng.2024.109126","url":null,"abstract":"<div><div>The effect of surface roughness on the detachment between the bubbles and the glass beads (soda-lime) was comprehensively investigated. Glass beads with dimensions of −1.20 + 1.12 mm were acid etched to achieve varying degrees of surface roughness, followed by silanation reactions conducted for different immersion times. The characterization of surface roughness was conducted using a ContourGT-K 3D optical microscope. Measurements of receding contact angle, induction time and detachment force were conducted to assess the influence of surface roughness on bubble and glass bead attachment/detachment. It is observed that the etching surface of glass beads with uniform protrusions and depressions, the hydrophobic glass beads exhibited shorter induction time, larger contact angle and higher critical detachment force. However, the stability of aggregates of bubbles and hydrophilic glass beads was reduced, making them prone to detachment. Moreover, larger protrusions and depressions on hydrophobic glass bead surfaces with increasing etching time, resulted in an increase in induction time, a decrease in receding contact angle and critical detachment force. The stability of bubbles and hydrophilic glass bead aggregates remained unchanged.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109126"},"PeriodicalIF":4.9,"publicationDate":"2024-11-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142747413","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Due to the strong natural floatability of molybdenite and talc, conventional flotation depressants are difficult to separate these two minerals. As a common depressant, starch has a strong inhibitory effect on both minerals (Castro et al., 2016), while sodium carboxymethyl cellulose has a weak inhibitory effect on both minerals (Chen et al., 2024). Therefore, selecting a proper depressant is the key for achieving the efficient flotation separation. This study investigated the flotation separation of talc and molybdenite using carrageenan as the depressant and sodium butyl xanthate (SBX) as the collector. The micro-flotation test results showed that carrageenan exhibited a strong depressing effect on both talc and molybdenite, and even stronger on molybdenite. However, molybdenite could achieve flotation after adding SBX, while talc was still suppressed. In addition, it was observed that the recovery of molybdenite by adding SBX first was higher than that of adding carrageenan first. A concentrate with a molybdenum grade of 50.64% and recovery of 87.34% was obtained in the artificial ore flotation with the initial grade of 28.52%. The adsorption mechanism of carrageenan on the surfaces of molybdenite and talc was studied using contact angle testing, adsorption capacity testing, zeta potential measurement, Scanning Electron Microscopy-Energy Dispersive Spectrometer (SEM-EDS) analysis, Fourier Transform Infrared Spectroscopy (FTIR) and X-ray Photoelectron Spectroscopy (XPS) analysis. It was concluded that carrageenan physically adsorbs on both mineral surfaces, whereas SBX adsorbs selectively on the surface of molybdenite and competes with carrageenan for adsorption.
辉钼矿和滑石具有较强的天然可浮性,常规浮选抑制剂难以将两者分离。淀粉作为一种常见的抑制剂,对这两种矿物质都有较强的抑制作用(Castro et al., 2016),而羧甲基纤维素钠对这两种矿物质的抑制作用较弱(Chen et al., 2024)。因此,选择合适的抑制剂是实现浮选高效分离的关键。以卡拉胶为抑制剂,丁基黄药钠(SBX)为捕收剂,研究了滑石和辉钼矿的浮选分离。微浮选试验结果表明,卡拉胶对滑石和辉钼矿均有较强的抑制作用,对辉钼矿的抑制作用更强。而加入SBX后辉钼矿可实现浮选,而滑石仍有抑制作用。另外,先加入SBX的辉钼矿回收率高于先加入卡拉胶的辉钼矿回收率。人工浮选获得了钼品位为50.64%、钼回收率为87.34%的精矿,初始品位为28.52%。采用接触角测试、吸附量测试、zeta电位测试、扫描电镜-能谱仪(SEM-EDS)分析、傅里叶变换红外光谱(FTIR)分析和x射线光电子能谱(XPS)分析等方法研究了卡拉胶在辉钼矿和滑石表面的吸附机理。结果表明,卡拉胶在辉钼矿表面均有吸附作用,而SBX则在辉钼矿表面选择性吸附,并与卡拉胶竞争吸附。
{"title":"Flotation separation of molybdenite from talc using carrageenan as depressant","authors":"Chao Li, Chao Wang, Fei Wu, Guangli Zhu, Yijun Cao, Shaohang Cao","doi":"10.1016/j.mineng.2024.109122","DOIUrl":"10.1016/j.mineng.2024.109122","url":null,"abstract":"<div><div>Due to the strong natural floatability of molybdenite and talc, conventional flotation depressants are difficult to separate these two minerals. As a common depressant, starch has a strong inhibitory effect on both minerals (<span><span>Castro et al., 2016</span></span>), while sodium carboxymethyl cellulose has a weak inhibitory effect on both minerals (<span><span>Chen et al., 2024</span></span>). Therefore, selecting a proper depressant is the key for achieving the efficient flotation separation. This study investigated the flotation separation of talc and molybdenite using carrageenan as the depressant and sodium butyl xanthate (SBX) as the collector. The micro-flotation test results showed that carrageenan exhibited a strong depressing effect on both talc and molybdenite, and even stronger on molybdenite. However, molybdenite could achieve flotation after adding SBX, while talc was still suppressed. In addition, it was observed that the recovery of molybdenite by adding SBX first was higher than that of adding carrageenan first. A concentrate with a molybdenum grade of 50.64% and recovery of 87.34% was obtained in the artificial ore flotation with the initial grade of 28.52%. The adsorption mechanism of carrageenan on the surfaces of molybdenite and talc was studied using contact angle testing, adsorption capacity testing, zeta potential measurement, Scanning Electron Microscopy-Energy Dispersive Spectrometer (SEM-EDS) analysis, Fourier Transform Infrared Spectroscopy (FTIR) and X-ray Photoelectron Spectroscopy (XPS) analysis. It was concluded that carrageenan physically adsorbs on both mineral surfaces, whereas SBX adsorbs selectively on the surface of molybdenite and competes with carrageenan for adsorption.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"222 ","pages":"Article 109122"},"PeriodicalIF":4.9,"publicationDate":"2024-11-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142747412","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-11-26DOI: 10.1016/j.mineng.2024.109113
William Spencer, Don Ibana, Pritam Singh, Aleksandar N. Nikoloski
The use of coal for ilmenite reduction to produce synthetic rutile is widespread in industry. However, the carbon dioxide emissions associated with coal combustion pose significant environmental concerns. Alternative reductants such as hydrogen have the potential to promote environmentally friendly production of green rutile. This study aimed to assess the technical feasibility of reducing an Australian secondary (weathered) ilmenite using hydrogen, focusing on the effects of reduction temperature and time. The ilmenite was composed of 65 % titanium dioxide, 29 % iron oxide, and 6 % impurities. Samples at each stage of the processing were analysed using X-ray fluorescence spectrometry (XRF) and scanning electron microscopy (SEM). The results revealed that both temperature and time impacted ilmenite reduction, with increasing values of both parameters leading to higher reduction percentages. The maximum reduction percentages were obtained for a reduction time of 240 min at all temperatures, and there was an increase from 62 % at 973 K to 99 % at 1273 K for this reduction time. A reduction percentage of 90 % was obtained at 1273 K with a holding time of 60 min. This study indicates that a minimum temperature of 1073 K is required to achieve a reduction exceeding 90 % for secondary ilmenite. The SEM analysis showed that fine, discrete, metallised iron particles were present on the surface of the reduced secondary ilmenite. The investigation into hydrogen as an alternative reductant demonstrated improved iron–titanium separation in acid leaching compared with the conventional reduction method using coal and resulted in green rutile products with titanium dioxide grades exceeding 96 %, and iron oxide content below 1 %.
工业上普遍使用煤来还原钛铁矿以生产合成金红石。然而,与煤炭燃烧相关的二氧化碳排放会带来严重的环境问题。氢气等替代还原剂有可能促进环保型绿色金红石的生产。本研究旨在评估使用氢气还原澳大利亚二级(风化)钛铁矿的技术可行性,重点关注还原温度和时间的影响。钛铁矿由 65% 的二氧化钛、29% 的氧化铁和 6% 的杂质组成。使用 X 射线荧光光谱仪(XRF)和扫描电子显微镜(SEM)分析了每个加工阶段的样品。结果表明,温度和时间都会影响钛铁矿的还原,这两个参数值越大,还原率越高。在所有温度下,当还原时间为 240 分钟时,还原率最高,从 973 K 时的 62% 增加到 1273 K 时的 99%。在保持 60 分钟的情况下,1273 K 的还原率为 90%。这项研究表明,要使二次钛铁矿的还原率超过 90%,最低温度为 1073 K。扫描电镜分析表明,还原后的二次钛铁矿表面存在细小、离散的金属化铁颗粒。对氢气作为替代还原剂的研究表明,与使用煤炭的传统还原方法相比,在酸浸出过程中铁钛分离效果更好,生产出的绿色金红石产品二氧化钛品位超过 96%,氧化铁含量低于 1%。
{"title":"Producing green rutile from secondary ilmenite via hydrogen reduction","authors":"William Spencer, Don Ibana, Pritam Singh, Aleksandar N. Nikoloski","doi":"10.1016/j.mineng.2024.109113","DOIUrl":"10.1016/j.mineng.2024.109113","url":null,"abstract":"<div><div>The use of coal for ilmenite reduction to produce synthetic rutile is widespread in industry. However, the carbon dioxide emissions associated with coal combustion pose significant environmental concerns. Alternative reductants such as hydrogen have the potential to promote environmentally friendly production of green rutile. This study aimed to assess the technical feasibility of reducing an Australian secondary (weathered) ilmenite using hydrogen, focusing on the effects of reduction temperature and time. The ilmenite was composed of 65 % titanium dioxide, 29 % iron oxide, and 6 % impurities. Samples at each stage of the processing were analysed using X-ray fluorescence spectrometry (XRF) and scanning electron microscopy (SEM). The results revealed that both temperature and time impacted ilmenite reduction, with increasing values of both parameters leading to higher reduction percentages. The maximum reduction percentages were obtained for a reduction time of 240 min at all temperatures, and there was an increase from 62 % at 973 K to 99 % at 1273 K for this reduction time. A reduction percentage of 90 % was obtained at 1273 K with a holding time of 60 min. This study indicates that a minimum temperature of 1073 K is required to achieve a reduction exceeding 90 % for secondary ilmenite. The SEM analysis showed that fine, discrete, metallised iron particles were present on the surface of the reduced secondary ilmenite. The investigation into hydrogen as an alternative reductant demonstrated improved iron–titanium separation in acid leaching compared with the conventional reduction method using coal and resulted in green rutile products with titanium dioxide grades exceeding 96 %, and iron oxide content below 1 %.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"221 ","pages":"Article 109113"},"PeriodicalIF":4.9,"publicationDate":"2024-11-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142698112","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}
Pub Date : 2024-11-26DOI: 10.1016/j.mineng.2024.109131
Dashi Lei , Yuen Yan , Songbo Ma , Xiaoliang Zhang , Xiangyu Peng , Yubin Wang , Yangge Zhu
The oxidation of molybdenite in water-oxygen system adversely affects the flotation recovery. However, previous studies primarily focused on the oxidation of MoS2 edge surfaces, neglecting the oxidation of basal facets, which constitute a larger proportion of the overall surface area. In this work, we systematically investigated the oxidation behavior of the molybdenite base surface and explored the influence of base surface oxidation sites on flotation behavior. The results demonstrated that surface oxidation of molybdenite leaded to a negative surface potential, decreased hydrophobicity and reduced dodecane adsorption. Electrostatic potential (ESP) and density functional theory (DFT) calculations revealed that oxidation sites on the molybdenite surface exhibited a strong negative charge, enhancing the adsorption of water molecules while weakening kerosene adsorption. Molecular dynamics (MD) simulations indicated that the oxidized molybdenite surface formed a hydration layer with thickness of ∼ 6 nm, which impedes dodecane adsorption. Moreover, this study proposed an effective strategy to improve molybdenite flotation recovery, that is reducing the concentration of dissolved oxygen in the pulp to inhibit MoS2 oxidation. These findings provide new insights into the oxidation behavior of molybdenite, and contribute to a better understanding of its flotation behavior in pulp.
{"title":"New insights into the significant drop of molybdenite flotation Recovery: The Overlooked oxidation of MoS2 basal facet","authors":"Dashi Lei , Yuen Yan , Songbo Ma , Xiaoliang Zhang , Xiangyu Peng , Yubin Wang , Yangge Zhu","doi":"10.1016/j.mineng.2024.109131","DOIUrl":"10.1016/j.mineng.2024.109131","url":null,"abstract":"<div><div>The oxidation of molybdenite in water-oxygen system adversely affects the flotation recovery. However, previous studies primarily focused on the oxidation of MoS<sub>2</sub> edge surfaces, neglecting the oxidation of basal facets, which constitute a larger proportion of the overall surface area. In this work, we systematically investigated the oxidation behavior of the molybdenite base surface and explored the influence of base surface oxidation sites on flotation behavior. The results demonstrated that surface oxidation of molybdenite leaded to a negative surface potential, decreased hydrophobicity and reduced dodecane adsorption. Electrostatic potential (ESP) and density functional theory (DFT) calculations revealed that oxidation sites on the molybdenite surface exhibited a strong negative charge, enhancing the adsorption of water molecules while weakening kerosene adsorption. Molecular dynamics (MD) simulations indicated that the oxidized molybdenite surface formed a hydration layer with thickness of ∼ 6 nm, which impedes dodecane adsorption. Moreover, this study proposed an effective strategy to improve molybdenite flotation recovery, that is reducing the concentration of dissolved oxygen in the pulp to inhibit MoS<sub>2</sub> oxidation. These findings provide new insights into the oxidation behavior of molybdenite, and contribute to a better understanding of its flotation behavior in pulp.</div></div>","PeriodicalId":18594,"journal":{"name":"Minerals Engineering","volume":"221 ","pages":"Article 109131"},"PeriodicalIF":4.9,"publicationDate":"2024-11-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"142698113","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}