Hydrometallurgy最新文献

{"title":"Study on pre-oxidation of silver concentrate and leaching behaviour of Zn, Cu and In during oxygen-pressure leaching","authors":"Liu Qiang,&nbsp;Li Cun-xiong ,&nbsp;Gu Zhi-hui,&nbsp;Li Chang-wen,&nbsp;Wang Qi-liang","doi":"10.1016/j.hydromet.2024.106358","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106358","url":null,"abstract":"<div><p>Given the limitations of current processing methods and the potential of high recovery of silver as a flotation concentrate, this study proposes a pre-oxidation followed by oxygen pressure sulphuric acid leaching route for zinc, copper and indium and thoroughly examines the alteration in micro-morphology of the silver concentrate of 1.22% Pb, 3010 g/t Ag and 649 g/t In. Under the optimal conditions of a sulphuric acid pre-oxidation temperature of 60 °C, and an acid-to-ore mass ratio of 0.6, over 15 h, the P<img>O and -OH polar groups of flotation reagents on the surface of silver concentrate particles are effectively neutralized through sulphuric acid oxidation. This action prevents the formation of a hydration film and mineral inclusions, thereby facilitating the efficient leaching of valuable elements. With a set reaction temperature of 155 °C, an initial acidity of 160 g/L, a reaction time of 180 min, an oxygen partial pressure of 0.8 MPa and a liquid-to-solid ratio of 7 mL/g, the leaching efficiency of Zn, Cu and In in the silver concentrate reach 94.8%, 98.4% and 91.1%, respectively while the lead and silver grades in the leach residue increase to 2.88% and 7754 g/t, respectively.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.8,"publicationDate":"2024-06-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141583083","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}

{"title":"Cesium extraction from an alkali-free solution using a 4-tert-butyl-2-(α-methylbenzyl) phenol–di-(2-ethylhexyl) phosphoric acid synergistic system: A conceptual process flowsheet for separating cesium salt from salt-lake brine","authors":"Xinyu Cheng ,&nbsp;Dong Shi ,&nbsp;Yuze Zhang ,&nbsp;Xiaowu Peng ,&nbsp;Shaolei Xie ,&nbsp;Lijuan Li ,&nbsp;Yong Niu ,&nbsp;Yuxuan Wang ,&nbsp;Fugen Song","doi":"10.1016/j.hydromet.2024.106353","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106353","url":null,"abstract":"<div><p>Cesium is an important strategic resource, and solvent extraction is the most frequently used technology for its extraction from various minerals and brines. However, this common method faces operational and cost problems owing to large alkali consumption. A synergistic extraction system consisting of 4-<em>tert</em>-butyl-2-(α-methylbenzyl) phenol (t-BAMBP) and di-(2-ethylhexyl) phosphoric acid (D2EHPA) was designed and used to extract Cs⁺ from an alkali-free solution. The effects of variables such as: (i) pH, (ii) concentration of t-BAMBP and D2EHPA, (iii) temperature, (iv) Cs⁺ concentration, and (v) coexisting cations, on the Cs⁺ extraction performance of the synergistic system were investigated. The most suitable organic phase composition was 1.0 mol/L t-BAMBP and 0.1 mol/L D2EHPA in kerosene, and the synergistic coefficient was up to 57 at 25 °C and an organic/aqueous phase volume ratio of 1/1. The extraction sequence of cations using the t-BAMBP–D2EHPA synergistic system followed the descending order Cs⁺ &gt; Rb⁺ &gt; Ca²⁺ &gt; K⁺ &gt; Li⁺ &gt; Mg²⁺ &gt; Na⁺. The chemical formula of the extracted species was determined as [CsA(HA)(ROH)₂] using the slope method. The Cs⁺ extraction process is an exothermic reaction with an enthalpy (<em>ΔH</em>^<em>o</em>) of −55.3 kJ mol⁻¹, confirmed by the thermodynamic study. After three-stage countercurrent extraction, the extraction efficiency of Cs⁺ was 92.6%, demonstrating excellent selectivity from coexisting cations. The t-BAMBP–D2EHPA synergistic system showed outstanding economic and environmental advantages and a good application prospect to develop a conceptual process flowsheet for extraction with this system and stripping with HCl to separate cesium salt from salt-lake brine.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.8,"publicationDate":"2024-06-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141539662","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}

{"title":"Production of α-Ti(HPO4)2·H2O, TiP2O7 and (TiO)2P2O7 from ilmenite by KOH roasting, H3PO4 leaching and calcination","authors":"Ushan S. Kulathunga ,&nbsp;Kusal D. Mendis ,&nbsp;Ashen I. Mapa ,&nbsp;Champa D. Jayaweera ,&nbsp;Masaru Shimomura ,&nbsp;Lalinda Palliyaguru ,&nbsp;Pradeep M. Jayaweera","doi":"10.1016/j.hydromet.2024.106354","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106354","url":null,"abstract":"<div><p>Alpha titanium bis(hydrogenphosphate) monohydrate, α-Ti(HPO₄)₂·H₂O, (α-TiP) is a precursor material utilized to obtain a broad range of important compounds having a great deal of applications ranging from ion-exchange chromatography, chemical catalysis to energy storage materials. The novel synthetic procedure developed in this study shows a higher conversion of titanium in ilmenite to α-TiP with a good purity. For the synthesis of TiPs, the direct use of natural ilmenite ore with commonly available chemicals such as KOH, H₃PO₄, HCl, and H₂C₂O₄ highlights the significance of the present investigation. A mixture of ilmenite and KOH with a molar ratio of 1:4 was roasted at 800<span><math><msup><mrow></mrow><mo>°</mo></msup><mi>C</mi></math></span> for 4 h to concentrate all the titanium to potassium titanate and iron to iron oxide. A reaction between potassium titanate and iron oxide with 85% (<em>w</em>/w) H₃PO₄ acid results in a leachate rich in iron in the form of soluble iron phosphates and a white precipitate identified as α-TiP. Calcination of α-TiP at 800<span><math><msup><mrow></mrow><mo>°</mo></msup><mi>C</mi></math></span> produces titanium pyrophosphate, TiP₂O₇. Residual iron that co-precipitated with α-TiP was further removed by multiple washing steps with complexing acids; H₃PO₄ or concentrated HCl. Washing with oxalic acid (H₂C₂O₄) produces a precipitate upon calcination identified as titanyl pyrophosphate, (TiO)₂P₂O₇. Flowcharts were developed and the chemical identities and the purity of the prepared α-Ti(HPO₄)₂·H₂O and (TiO)₂P₂O₇ were tested with X-ray diffraction, X-ray fluorescence, thermogravimetric, and Raman spectroscopic techniques.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.8,"publicationDate":"2024-06-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141486524","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}

{"title":"A hydrometallurgical process flowsheet for recovering MoO3 from Molybdenite","authors":"Hossein Shalchian ,&nbsp;Ionela Birloaga ,&nbsp;Motahareh Bagheri Moghaddam ,&nbsp;Hadi Nasiri ,&nbsp;Francesco Vegliò","doi":"10.1016/j.hydromet.2024.106355","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106355","url":null,"abstract":"<div><p>In this study, a comprehensive hydrometallurgical processing of molybdenite (MoS₂) concentrate was investigated. This investigation involved a novel approach combining mechanical activation, leaching, and polyelectrolyte extraction methods. The integrated method effectively addressed the challenge of low leaching rate of molybdenite, resulting in the successful production of high-purity molybdenum trioxide. Milled molybdenite samples were analyzed by different methods of X-ray diffraction, atomic force and electron microscopy, and BET. The increasing trend of the specific surface area during milling was determined by a model fitting which was useful for optimization of milling time. Several leaching reagents were studied to achieve high molybdenum dissolution. The most promising results were achieved through a two-hour process, yielding an impressive leaching efficiency of 80% and a resulting Mo concentration of 6700 mg/L. Molybdenum recovery was efficiently carried out through polyelectrolyte extraction, as confirmed by ICP and CHNS analyses, demonstrating selective precipitation of molybdenum from the solution. The subsequent calcination of the precipitated molybdenum(VI) compound resulted in the production of high-purity molybdenum trioxide. Furthermore, a conceptual hydrometallurgical treatment process for molybdenite concentrate was proposed, aiming to recover molybdenum, sulfuric acid, and copper. This proposed process presents a promising avenue for further exploration in pilot plant studies within the molybdenum industry.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.8,"publicationDate":"2024-06-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141438352","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}

{"title":"Influence of ionic liquid (R4PSCN) for selective separation and recovery of copper from spent CuCr catalyst leach liquor","authors":"Saroj Sekhar Behera ,&nbsp;Pankaj Kumar Parhi","doi":"10.1016/j.hydromet.2024.106352","DOIUrl":"10.1016/j.hydromet.2024.106352","url":null,"abstract":"<div><p>Separation and recovery of copper (Cu) from sulphate mediated Cu<img>Cr spent catalyst leach solution through solvent extraction approach has been systematically investigated. A number of Ionic Liquid (IL) and other conventional extractants were used while investigating the selectivity and efficient extraction tendency of either IL or extractants towards Cu(II). In context of copper extraction efficiency, the adopted organic reagents followed the descending order: R₄PSCN &gt; R₄PD &gt; R₄PCy &gt; Cyphos 101 &gt; Aliquot 336 &gt; D2EHPA &gt; Cyanex 272. The extraction behavior of Cu(II) was established based on slope analysis method. From the results it was noticed that extraction occurs through a cation exchange mechanism with association of a mole of Cu(II) per mole of R₄PSCN. The plot of log D vs. log [R₄PSCN] yield a linear relationship with a slope close to 4 which is used to propose extraction reaction mechanism/ stoichiometry. The nature of complex between Cu(II) and IL was further examined using FTIR analysis of the loaded organic phase with the diluent. Mc-Cabe Thiele diagram was constructed to predict quantitative extraction of Cu(II) which revealed the need for two stages at aqueous to organic (A:O) phase volume ratio of =3:1. The stripping isotherm constructed at optimum NH₄OH concentration (0.4 M) suggests the need for two stages at O:A phase volume ratio of = 2:1 for complete stripping of copper with regeneration of R₄SCN for further use. Both isotherm conditions were validated by 6 cycles of counter current simulation (CCS) study for obtaining the desired amount of Cu(II) loaded R₄SCN (during extraction) and/or stripped copper solution (during stripping). Overall copper enrichment was ∼6 fold leading to produce a copper(II) solution of 48 g/L from 6 g/L Cu(II). The stripped solution was subjected to crystallization study to produce copper sulphate crystals of high purity and was confirmed by XRD analysis of crystal phases.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.7,"publicationDate":"2024-06-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141399277","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}

{"title":"Efficient extraction of lithium from alkaline solution using the synergistic extractants ethylhexyl salicylate and trialkylphosphine oxide in kerosene and stripping with acid","authors":"Zhonghua Niu ,&nbsp;Licheng Zhang ,&nbsp;Ruirui Liu ,&nbsp;Yongquan Zhou ,&nbsp;Lianmin Ji ,&nbsp;Lijuan Li","doi":"10.1016/j.hydromet.2024.106342","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106342","url":null,"abstract":"<div><p>Efficient separation of lithium from alkaline solution with high Na/Li ratio is of great importance for the development of batteries for new energy industry. This work proposes the use of a novel extraction system composed of ethylhexyl salicylate (ES) and trialkylphosphine oxide (TRPO). The equilibrium experiment revealed that the order of metal ions extracted by ES/TRPO extraction system is Mg²⁺ &gt; Ca²⁺ &gt; Li⁺ &gt; Na⁺ &gt; K⁺. A recovery process including extraction, scrubbing, and stripping was designed to recover lithium from a solution of 3.25 g/L Li, 52 g/L Na and 0.8 mol/L OH⁻. More than 99% of lithium could be extracted to the organic phase. After stripping, a lithium-rich solution containing 25 g/L Li was obtained, and the system showed good stability in the cycling experiments. The FT-IR analysis and DFT calculation were conducted to investigate the extraction mechanism. The results demonstrated that ES mainly coordinates with metal ions through Ph-O and C<img>O bonds to form a hexatomic ring complex, thereby allowing metal ions to enter the organic phase. The calculated binding energies of the complex are highly consistent with the equilibrium experiment. The present work may provide a novel extraction system to efficiently recover lithium from alkaline solution with high Na/Li ratio.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.7,"publicationDate":"2024-05-31","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141286300","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}

{"title":"Base metals recovery from waste printed circuit board leachate using biogenic hydrogen sulfide gas","authors":"Jonovan Van Yken ,&nbsp;Naomi J. Boxall ,&nbsp;Ka Yu Cheng ,&nbsp;Aleksandar N. Nikoloski ,&nbsp;Navid R. Moheimani ,&nbsp;Anna H. Kaksonen","doi":"10.1016/j.hydromet.2024.106341","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106341","url":null,"abstract":"<div><p>Electronic waste, or e-waste, represents one of the rapidly expanding categories of waste worldwide. By 2019, the global production of e-waste had surged to 53.6 million tons. Due to its substantial metal content, e-waste holds significant financial value, estimated at US$57 billion globally in 2019, predominantly concentrated in printed circuit boards (PCBs). Previous studies have explored hydrometallurgy techniques to extract base metals from PCBs, but effectively recovering these solubilised metals remained a challenge. This research sought to assess metal recovery from PCB waste leachate by utilising hydrogen sulfide generated through a consortium of sulfate-reducing bacteria (SRB) in a fluidised bed reactor (FBR). Both lactate and glycerol were examined as potential organic electron donors for the sulfate reduction. With lactate (1 g L⁻¹) as the electron donor, the FBR achieved an average sulfate reduction efficiency of 62%, with a hydrogen sulfide (H₂S) production rate of 250 mg H₂S-S L⁻¹ d⁻¹ and H₂S-S concentration of 300 mg L⁻¹ in the effluent. When glycerol was the organic electron donor, the average sulfate reduction efficiency was 49%, H₂S production rate was 210 mg H₂S-S L⁻¹ d⁻¹ and H₂S-S concentration was 260 mg L⁻¹. <em>Desulfovibrio</em>, <em>Desulfococcus</em> and <em>Desulfomicrobium</em> were the dominant sulfate reducers in the FBR. The resulting dissolved hydrogen sulfide was employed to recover metals from e-waste leach liquor. Utilising biogenic sulfide and NaOH, a notably high precipitation efficiency (&gt;99%) was attained for aluminum, nickel, copper, and zinc. Additionally, iron, utilised in the e-waste leaching process, was also recovered with an efficiency exceeding 99%. The precipitation of metals occurred within a pH range from 1.5 to 8.5. Overall, this process facilitated the formation of valuable mixed-metal precipitates from waste PCB-derived leachate. These precipitates could undergo further purification or serve as raw material for subsequent processes.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.7,"publicationDate":"2024-05-29","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S0304386X24000811/pdfft?md5=5c54645e11e05d5f355e7239d8a80307&pid=1-s2.0-S0304386X24000811-main.pdf","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141286114","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}

{"title":"High efficiency separation of bastnaesite (REFCO3) and monazite (REPO4) in mixed rare earth concentrate by heating under N2 and leaching with HCl/AlCl3","authors":"Jiahao He ,&nbsp;Peng Gao ,&nbsp;Shuai Yuan ,&nbsp;Shaokai Cheng ,&nbsp;Jilai Ning ,&nbsp;Zhenya Zhou ,&nbsp;Yongsheng Sun ,&nbsp;Wenbo Li","doi":"10.1016/j.hydromet.2024.106338","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106338","url":null,"abstract":"<div><p>Bayan Obo mixed rare earth (RE) concentrate is one of the most significant rare earth mineral resources worldwide. However, the concentrated sulfuric acid roasting method, which is commonly used to treat ores, generates pollutants such as waste gas, wastewater, and leach residue, resulting in the squandering of the associated resources. This paper introduces a green process involving selective mineral phase transformation (MPT) by heating, followed by leaching to separate bastnaesite and monazite in a mixed RE concentrate to facilitate their subsequent decomposition or extraction. The effects of the MPT conditions on rare earth extraction were investigated. During the MPT process, bastnasite decomposed into REOF, which is more easily leached, whereas monazite remained unchanged. Under suitable conditions, the leaching efficiency of REOF reached 93.7%, while that of monazite (REPO₄) was only 3.2%. Furthermore, the content of monazite in the leach residue was 91.2%. Compared to the mixed RE concentrate, numerous cracks and pores were generated on the surface and inside the MPT products. Furthermore, the total pore volume and specific surface area significantly increased, which made the reaction between the MPT products and hydrochloric acid more efficient. Thus, the MPT process facilitated the leaching of bastnasite and its separation from monazite.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.7,"publicationDate":"2024-05-28","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141324236","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}

{"title":"Investigating the mechanism of Au(III) transport using a polymer inclusion membrane with dibutyl carbitol as a carrier","authors":"Meisam Ghiasi ,&nbsp;Mahmoud Abdollahy ,&nbsp;Mahdi Abdollahi ,&nbsp;Mehdi Mohseni","doi":"10.1016/j.hydromet.2024.106339","DOIUrl":"https://doi.org/10.1016/j.hydromet.2024.106339","url":null,"abstract":"<div><p>In this article, firstly, the separation and transfer of Au(III) from gold chloride solution was investigated using a polymer inclusion membrane (PIM) system containing dibutyl carbitol (DBC) as carrier molecules, dioctyl phthalate (DOP), bis(2-ethyl hexyl) adipate (dioctyl adipate) (DOA) and tris (2-ethyl hexyl) phosphate (T2EHP) as plasticizers and high molecular weight polyvinyl chloride (PVC) as the base polymer. Fourier transform infrared spectroscopy (FT-IR), and scanning electron microscope (SEM) were used to identify PIMs. Kinetic studies featuring a two-step reaction, with the first step being reversible, were conducted across various sections to investigate the processes of extraction, stripping, and transport. The effects of different stripping agents such as water, HCl, thiourea, sodium thiosulfate, and oxalic acid was investigated, and the best results were obtained with thiourea. Also, the mechanisms of Au(III) extraction and transport were studied. Under the conditions of source solution, tetrachloroaurate anionic complex <span><math><msup><mfenced><mrow><mi>Au</mi><msub><mi>Cl</mi><mn>4</mn></msub></mrow></mfenced><mo>−</mo></msup></math></span> with protonated DBC (<span><math><msubsup><mfenced><mrow><msub><mfenced><mi>ROR</mi></mfenced><mn>2</mn></msub><mi>OH</mi></mrow></mfenced><mfenced><mi>M</mi></mfenced><mo>+</mo></msubsup></math></span>) was extracted by ion solvation mechanism. The validity of the proposed extraction mechanism was confirmed through the use of nuclear magnetic resonance (¹H NMR) spectroscopy. In order to make the membrane with the best composition and the highest efficiency, the effect of weight percentage of the carrier and plasticizer was investigated. There was an optimal value for the weight percentage of plasticizer (10–20% by weight) and carrier (40%), in which the highest flux and permeability in the membrane occurred. The effect of the viscosity of different plasticizers (DOP, DOA, and T2EHP) on the Au(III) flux was also investigated. It was found that the flux increases linearly with the reduction of plasticizer viscosity. Effect of membrane thickness on the permeability, initial flux, and efficiency of Au(III) transfer, were conducted with thickness of 120, 80, 45, and 30 μm. By reducing the thickness of the membrane, the transfer flux, permeability and percent of Au(III) transport, were improved from 12.9 × 10⁻³ <span><math><mi>m</mi><mspace></mspace><msup><mi>h</mi><mrow><mo>−</mo><mn>1</mn></mrow></msup></math></span>, 45.3 × 10⁻⁷ <span><math><mi>mol</mi><mspace></mspace><msup><mi>m</mi><mrow><mo>−</mo><mn>2</mn></mrow></msup><mspace></mspace><msup><mi>s</mi><mrow><mo>−</mo><mn>1</mn></mrow></msup></math></span> and 18.2% to 26.4 × 10⁻³ <span><math><mi>m</mi><mspace></mspace><msup><mi>h</mi><mrow><mo>−</mo><mn>1</mn></mrow></msup></math></span>, 83.5 × 10⁻⁷ <span><math><mi>mol</mi><mspace></mspace><msup><mi>m</mi><mrow><mo>−</mo><m","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.7,"publicationDate":"2024-05-26","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141243703","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}

{"title":"Hollow drop bubbles: A preliminary study of simplified prototype for improving copper(II) extraction with ACORGA® M5640 using coated bubble swarm","authors":"Diego Poblete ,&nbsp;Claudio Leiva ,&nbsp;María Sinche-Gonzalez ,&nbsp;Claudio Acuña","doi":"10.1016/j.hydromet.2024.106340","DOIUrl":"10.1016/j.hydromet.2024.106340","url":null,"abstract":"<div><p>There are two well-defined processes for the types of copper ores. One for the processing of copper sulfides and another for the processing of the copper oxides. There are similarities between the two, particularly in the preparation stage of the run of mine (ROM) such as the crushing. However, significant differences exist in how to concentrate the elements of interest. Flotation is the most used concentration process to separate copper sulfide minerals from other minerals using air bubbles. For oxides, after the dissolution of copper, the solvent extraction (SX) process is the preferred path using two immiscible liquids to separate the copper.</p><p>A line of investigation for solvent extraction is the use of a bubble coated with solvent to extract the metal of interest from the aqueous solution, some devices have been built and tested for this purpose using different principles to generate a coated bubble swarm. However, those equipments have been tested on laboratory and have not been scaled up to an industry level.</p><p>The Hollow Drop (HD) concept was born from the idea of building a device to generate coated bubbles in a continuous swarm that could be scalable to an industry level. In this paper two columns were built and operated: a proof-of-concept column and a scale-up attempt for the extraction of Cu(II) fom an aqueous solution of 2.5 g L⁻¹ using ACORGA® M5640 (25% <em>v</em>/v) in the Kerosene.</p><p>The results show that we could generate a bubble swarm and conduct the solvent extraction process at a 97% recovery using our proposed coated bubble generator. However, in our scaled prototype test only a 70% recovery was achieved, which shows that our column is working but the scaling-up needs more investigation regarding the dimensions and flows of the process.</p></div>","PeriodicalId":13193,"journal":{"name":"Hydrometallurgy","volume":null,"pages":null},"PeriodicalIF":4.7,"publicationDate":"2024-05-24","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://www.sciencedirect.com/science/article/pii/S0304386X2400080X/pdfft?md5=c37d7fbb4b8dae3a9d4322e028b88a13&pid=1-s2.0-S0304386X2400080X-main.pdf","citationCount":null,"resultStr":null,"platform":"Semanticscholar","paperid":"141143679","PeriodicalName":null,"FirstCategoryId":null,"ListUrlMain":null,"RegionNum":2,"RegionCategory":"材料科学","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":"OA","EPubDate":null,"PubModel":null,"JCR":null,"JCRName":null,"Score":null,"Total":0}