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<article article-type="research-article" dtd-version="1.3" xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xml:lang="en"><front><journal-meta><journal-id journal-id-type="publisher-id">gscience</journal-id><journal-title-group><journal-title xml:lang="en">Mining Science and Technology (Russia)</journal-title><trans-title-group xml:lang="ru"><trans-title>Горные науки и технологии</trans-title></trans-title-group></journal-title-group><issn pub-type="epub">2500-0632</issn><publisher><publisher-name>The National University of Science and Technology MISiIS (NUST MISIS)</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.17073/2500-0632-2024-03-229</article-id><article-id custom-type="elpub" pub-id-type="custom">gscience-673</article-id><article-categories><subj-group subj-group-type="heading"><subject>Research Article</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>BENEFICIATION AND PROCESSING OF NATURAL AND TECHNOGENIC RAW MATERIALS</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="ru"><subject>ОБОГАЩЕНИЕ, ПЕРЕРАБОТКА МИНЕРАЛЬНОГО И ТЕХНОГЕННОГО СЫРЬЯ</subject></subj-group></article-categories><title-group><article-title>“Invisible” noble metals in carbonaceous rocks and beneficiation products: feasibility of detection and coarsening</article-title><trans-title-group xml:lang="ru"><trans-title>«Невидимые» благородные металлы в углеродистых породах и продуктах обогащения: возможность выявления и укрупнения</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-3069-0001</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Александрова</surname><given-names>Т. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Aleksandrova</surname><given-names>Т.  N. </given-names></name></name-alternatives><bio xml:lang="ru"><p>Татьяна Николаевна Александрова – доктор технических наук, профессор, член-корреспондент РАН</p><p>Scopus ID 57216873316, ResearcherID A-5418-2014</p><p>г. Санкт-Петербург</p></bio><bio xml:lang="en"><p>Tayana N. Aleksandrova – Dr. Sci. (Eng.), Professor, Corresponding Member of the Russian Academy of Sciences</p><p>Scopus ID 57216873316, ResearcherID A-5418-2014</p><p>St. Petersburg</p></bio><email xlink:type="simple">Aleksandrova_TN@pers.spmi.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-8451-2489</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Афанасова</surname><given-names>А. В.</given-names></name><name name-style="western" xml:lang="en"><surname>Afanasova</surname><given-names>A.  V. </given-names></name></name-alternatives><bio xml:lang="ru"><p>Анастасия Валерьевна Афанасова – кандидат технических наук, доцент</p><p>Scopus ID 57188630049, ResearcherID AAH-4333-2019</p><p>г. Санкт-Петербург</p></bio><bio xml:lang="en"><p>Anastasia V. Afanasova – Cand. Sci. (Eng.), Associate Professor</p><p>Scopus ID 57188630049, ResearcherID AAH-4333-2019</p><p>St. Petersburg</p></bio><email xlink:type="simple">Afanasova_AV@pers.spmi.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-1364-5006</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Абурова</surname><given-names>В. А.</given-names></name><name name-style="western" xml:lang="en"><surname>Aburova</surname><given-names>V.  A. </given-names></name></name-alternatives><bio xml:lang="ru"><p>Валерия Александровна Абурова – аспирант</p><p>Scopus ID 57503048800</p><p>г. Санкт-Петербург</p></bio><bio xml:lang="en"><p>Valeria A. Aburova – PhD-Student</p><p>Scopus ID 57503048800</p><p>St. Petersburg</p></bio><email xlink:type="simple">aburovaleria@gmail.com</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff-alternatives id="aff-1"><aff xml:lang="ru">Санкт-Петербургский горный университет императрицы Екатерины II<country>Россия</country></aff><aff xml:lang="en">Empress Catherine II Saint Petersburg Mining University<country>Russian Federation</country></aff></aff-alternatives><pub-date pub-type="collection"><year>2024</year></pub-date><pub-date pub-type="epub"><day>20</day><month>09</month><year>2024</year></pub-date><volume>9</volume><issue>3</issue><fpage>231</fpage><lpage>242</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Aleksandrova Т.N., Afanasova A.V., Aburova V.A., 2024</copyright-statement><copyright-year>2024</copyright-year><copyright-holder xml:lang="ru">Александрова Т.Н., Афанасова А.В., Абурова В.А.</copyright-holder><copyright-holder xml:lang="en">Aleksandrova Т.N., Afanasova A.V., Aburova V.A.</copyright-holder><license license-type="creative-commons-attribution" xlink:href="https://creativecommons.org/licenses/by/4.0/" xlink:type="simple"><license-p>This work is licensed under a Creative Commons Attribution 4.0 License.</license-p></license></permissions><self-uri xlink:href="https://mst.misis.ru/jour/article/view/673">https://mst.misis.ru/jour/article/view/673</self-uri><abstract><p>The decrease in the quality of raw materials coming for processing requires involvement of refractory ores in processing, the refractoriness of which is caused by the presence of organic carbonaceous matter sorption-active in relation to dissolved noble metals and impregnation of fine noble metals in mineral-carriers. In this connection, the actual research line is the development of new technological solutions with the use of energy methods of action in order to reduce the losses of valuable components in beneficiation tailings. Treatment with ultra-high frequency electromagnetic radiation has a number of advantages, including rapid and selective heating due to the differences in the ability of minerals to absorb this radiation. Carbon-containing materials represented by carbonaceous flotation concentrate and model samples of activated carbon with adsorbed silver were taken as the research subjects. Using the model samples as an example, the necessity of using magnetite to achieve coarsening fine silver particles during ultra-high frequency treatment was substantiated. The formation of active centers of local heating during the treatment in the points of magnetite addition was confirmed. The necessary content of magnetite of 10% for coarsening fine silver to spherical aggregates, the average size of which was 20–40 microns, was substantiated. Coarsening noble metal particles to sizes of 20–50 microns in treated carbonaceous concentrates containing silver and gold was achieved, when the substantiated amount of magnetite was added. Coarsened particles (aggregates) of noble metals can be recovered using traditional beneficiation methods.</p></abstract><trans-abstract xml:lang="ru"><p>По причине снижения качества поступающего на переработку сырья, вовлечения упорных руд, упорность которых обусловлена наличием сорбционно-активного по отношению к растворенным благородным металлам органического углеродистого вещества и вкрапленностью низкоразмерных благородных металлов в минералы-носители, актуальным направлением является разработка новых технологических решений с применением энергетических методов воздействия с целью снижения потерь ценных компонентов с хвостами обогащения. Обработка электромагнитным излучением сверхвысокой частоты обладает рядом преимуществ, среди которых отмечаются быстрый и селективный нагрев за счет различий в способности поглощать минералами данное излучение. В качестве объекта исследования приняты углеродсодержащие материалы, представленные углеродистым флотационным концентратом и модельными навесками активированного угля с адсорбированным серебром. На примере модельных навесок обоснована необходимость использования магнетита для достижения укрупнения низкоразмерного серебра при сверхвысокочастотной обработке. Подтверждено образование активных центров локального нагрева в местах добавления магнетита в процессе обработки. Обосновано необходимое содержание магнетита для укрупнения низкоразмерного серебра до сферических агрегатов, средний размер которых составил 20–40 мкм, равное 10 %. Получено укрупнение частиц благородных металлов в обработанных углеродистых концентратах до размеров 20–50 мкм, содержащих серебро и золото, при добавлении обоснованного количества магнетита. Укрупненные частицы благородных металлов возможно извлекать с применением традиционных методов обогащения.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>СВЧ обработка</kwd><kwd>углеродистый концентрат</kwd><kwd>золотосодержащие руды</kwd><kwd>модельные навески</kwd><kwd>флотация</kwd><kwd>серебро</kwd><kwd>магнетит</kwd></kwd-group><kwd-group xml:lang="en"><kwd>microwave treatment</kwd><kwd>carbonaceous concentrate</kwd><kwd>gold-bearing ores</kwd><kwd>model samples</kwd><kwd>flotation</kwd><kwd>silver</kwd><kwd>magnetite</kwd></kwd-group><funding-group xml:lang="ru"><funding-statement>Работа выполнена в рамках гранта РНФ (проект № 23-47-00109).</funding-statement></funding-group><funding-group xml:lang="en"><funding-statement>The study was carried out within the framework of a grant from the Russian Science Foundation (Project No. 23-47-00109).</funding-statement></funding-group></article-meta></front><body><sec><title>“Invisible” noble metals in carbonaceous rocks and beneficiation products: feasibility of detection and coarsening</title></sec><sec><title>Introduction</title><p>The development of technologies for processing of strategic raw materials is necessary to maintain the world economy at the current level in connection with the depletion of mineral resource base. Worsening the quality of gold- and silver-containing raw materials, involvement of lean and refractory ores in processing owes the actualization of scientific research aimed at increasing the recovery of valuable components into concentrates [<xref ref-type="bibr" rid="cit1">1</xref>]. The analysis of existing studies has shown that some of the topical areas in the field of mineral beneficiation are increasing the efficiency of disintegration of mineral raw materials [2, 3], application of machine vision technology at various stages of beneficiation, synthesis of new flotation reagents [4–6], and the development of new reagent regimes [7–9].</p><p>The refractoriness of gold-bearing ores can be caused both by the presence of substances sorption-active in relation to dissolved gold and inclusions of fine noble metals in mineral-carriers, mainly in such minerals as pyrite, arsenopyrite, galena, etc. Ores in which both these features are present are referred to ores of double refractoriness. “Invisible” gold is referred to submicroscopic gold particles that are 1–100 nm in size and are not detected using optical or electron microscopy [<xref ref-type="bibr" rid="cit10">10</xref>]. The presence of “invisible” gold and silver in ores complicates the selection of flow charts for their processing and owes the necessity for the development of new process solutions and improvement of existing ones.</p><p>The carbonaceous material contained in the double-refractory ores contaminates the concentrates produced and results in significant losses of valuable components at the stage of metallurgical processing. The actual task of the existing research is to involve in processing carbonaceous products, going to tailings at most of the processing plants, in order to reduce losses of valuable components such as gold and silver [11–13].</p><p>In addition to native metal, silver in ores can be represented by dispersed inclusions in the host minerals, either as metallic or chemically bound silver. Chemically bound silver refers to various silver sulfides, for example, Ag2S. The presence of fine silver associated with sulfide minerals, as well as in the case of gold, complicates its recovery at the cyanidation stage [<xref ref-type="bibr" rid="cit14">14</xref>]. The recovery requires destruction of the matrix of the host minerals in order to provide the contact of reagents with the noble metal to dissolve it.</p><p>To date, there is a large amount of researches aimed at finding process solutions for the processing of refractory raw materials [15–17]. For double refractory ores, pretreatment to reduce the refractoriness of gold-bearing ores is required. The most common pretreatment methods are roasting, chlorination, pressure oxidation, bioleaching, and Albion technology. However, in addition to the traditional methods, research into the feasibility of using energy-based methods of action has become widespread [18, 19]. Ultra-high frequency (UHF) treatment is one of the promising methods whose advantages include fast and selective heating [20–22]. The selectivity of heating minerals is due to the differences in their heating rate, which in turn is connected with specific heat capacity, specific thermal conductivity, and relative dielectric constant. Recent researches with the use of microwave treatment are aimed at increasing the efficiency of disintegration of mineral raw materials [23-25], studying the feasibility of using microwaves for sorting ores [<xref ref-type="bibr" rid="cit26">26</xref>], reducing the content of harmful impurities in ores [<xref ref-type="bibr" rid="cit27">27</xref>], studying the effect on surface properties and flotability of minerals [<xref ref-type="bibr" rid="cit28">28</xref>], involvement of cyanide [<xref ref-type="bibr" rid="cit29">29</xref>] and sulfide [<xref ref-type="bibr" rid="cit30">30</xref>] tailings in the treatment. The melting temperature of “invisible” noble metals is much lower than the melting temperature of visible particles that predetermines the feasibility of their coarsening in the process of energy actions. For example, for Au, the melting point of a 1.6 nm diameter cluster is 257.85 °C [<xref ref-type="bibr" rid="cit33">33</xref>], while that of a 1.9 nm diameter cluster is 318.85 °C [<xref ref-type="bibr" rid="cit34">34</xref>]. For Ag, the melting point of a 4 nm diameter cluster is 449.85 °C [<xref ref-type="bibr" rid="cit5">5</xref>], while that of a 5 nm diameter cluster is 509.85 °C [<xref ref-type="bibr" rid="cit34">34</xref>]. Carbonaceous flotation products, as a rule, contain insignificant amounts of ore minerals, which requires sufficiently long time for microwave treatment in order to coarsen the particles. In this regard, the addition of magnetite in the process of treatment allows the creation of local heating centers. Table 1 systematizes the data of dependence of the achieved maximum heating temperature on the treatment time for sulfide mineral-concentrators of gold and products of their destruction after roasting.</p><p>Analysis of historical studies confirms the fact that magnetite is more active in relation to ultra-high frequency electromagnetic radiation and, in comparison with other minerals, reaches significantly higher heating temperatures. The low melting temperature of silver nanoclusters confirms the prospect of investigating the feasibility of their coarsening, since it is lower than the magnetite treatment heating temperature.</p><p>Thus, the purpose of this study was to reveal the mechanism of coarsening fine silver in the course of microwave treatment with the addition of magnetite using model samples and to justify the required content of magnetite to confirm the feasibility of silver coarsening in the course of microwave treatment of carbonaceous flotation concentrate samples to reduce losses of valuable components in tailings. </p><p>Table 1</p><p>Summary data on dependence of maximum microwave heating temperature on treatment time</p></sec><sec><title>Research Materials and Techniques</title></sec><sec><title>1. Characterization of research subjects</title><p>The following carbon-containing materials were chosen as the research subjects:</p><p>The source of silver in the model sample was silver leaf, containing 99.9% Ag. Preparation of the model samples included: grinding of activated carbon, preparation of leaching solution, transition of silver leaf to liquid phase for two days (leaching), its subsequent contacting with activated carbon for three days. The leaching reagent is a mixture of iodine complex, amino acids, sodium chloride, urea, ammonium chloride, and sodium carbonate. After contacting the noble metal with activated carbon, filtration and drying of the obtained cake was carried out for subsequent microwave treatment.</p><p>The initial carbonaceous gold-bearing ore is characterized by the presence of fine inclusions of gold and insignificant amount of silver in the mineral-concentrators, such as pyrite and arsenopyrite, as well as organic carbonaceous matter sorption-active in relation to dissolved gold. The main valuable component is gold, the grade of which in the initial ore is 5.99 ± 0.29 g/t. Silver is a by-product, the grade of which is 0.29 ± 0.1 g/t.</p></sec><sec><title>2. Flotation beneficiation experiments</title><p>Separation of carbonaceous flotation concentrate from refractory gold-bearing ore was carried out using pneumomechanical flotation machine Flotation Bench Test Machine of Laarmann company with cell volume of 1.5 liters. The initial ore was subjected to grinding to particle size of 60% passing 71 μm, after which carbonaceous flotation was carried out with the addition of oxal frothing agent, the consumption of which was 85 g/t. The results of studying the obtained flotation products are presented in Table 2.</p><p>The obtained carbonaceous flotation concentrate after drying was subjected to microwave treatment, while the tailings of carbonaceous flotation went for additional grinding and subsequent sulfide flotation.</p><p>Table 2</p><p>Results of research of refractory gold-bearing ore flotation products</p></sec><sec><title>3. Microwave treatment</title><p>Microwave treatment of carbon-containing materials without and with the addition of different amount of magnetite (3, 5, 10, 15% by weight of a sample) was carried out using a Sineo UWave-2000 microwave oven, the range of possible setting of power in which was 100–1000 W. The coarseness of the added magnetite was −50 μm.</p></sec><sec><title>4. Scanning electron microscopy</title><p>In order to confirm coarsening fine silver in model samples and carbonaceous flotation concentrate after microwave treatment with the addition of magnetite to create active centers of local heating, the study of the samples before and after the treatment was carried out using a Vega 3 LMH scanning electron microscope, combined with a system of X-ray energy dispersive microanalysis Oxford Instruments INCA Energy 250/X-max 20. The fine silver coarsening study was carried out with the determination of sizes of a minimum of 200 particles in each of the samples obtained. The carbonization of the samples was carried out using a Q150R E sputtering apparatus manufactured by Quorum Technologies Ltd.</p></sec><sec><title>5. Microwave heating temperature</title><p>Measuring the achieved temperature of microwave heating of samples was carried out using a FinePower DIN21H laser pyrometer. The measuring temperature range was −50 to 1,100 °C with an accuracy of ±2%.</p></sec><sec><title>Findings and Discussion</title></sec><sec><title>1. Processing of silver-containing model samples without magnetite addition</title><p>In order to confirm the feasibility of coarsening fine silver in the course of microwave treatment, an initial model sample with adsorbed silver before treatment was studied for comparison. Figure 1 shows the results of the sample study before treatment using scanning electron microscopy. Table 3 shows the findings of the elemental composition study for the spectrum shown in Fig. 1.</p><p>Based on the results obtained, the absence of visible silver was revealed, which was confirmed by the results of the elemental composition study, thus confirming its “invisibility”.</p><p>Fig. 1. Results of investigation of the initial model sample before microwave treatment using scanning electron microscopy</p><p>Table 3</p><p>The results of the study of elemental composition for the spectra presented in Fig. 1</p><p>In order to confirm the necessity of adding magnetite to silver-containing model samples at microwave treatment for coarsening fine silver, the studies were carried out on model samples without magnetite addition. Figure 2 shows the results of scanning electron microscopy examination of the treated samples without magnetite addition. The results of the study of the elemental composition for the spectra in the studied samples are shown in Table 4.</p><p>Fig. 2. Results of scanning electron microscopy study of model samples with coarsened silver after microwave treatment without magnetite addition</p><p>Table 4</p><p>The results of the study of elemental composition for the spectra presented in Fig. 2</p><p>The analysis of the obtained data allowed confirming the feasibility of coarsening fine silver particles using microwave treatment without addition of magnetite up to the average size equal to 5–10 microns. Despite the fact that coarsening is achieved at the treatment without the addition of magnetite, the coarseness achieved in these studies does not allow extracting coarsened particles by traditional beneficiation methods. This fact predetermines the need to study the effect of the addition of different magnetite amounts to the studied model samples on coarsening fine silver particles.</p></sec><sec><title>2. Processing of silver-containing model samples with magnetite addition</title><p>The studies aimed at establishing the necessary magnetite content to achieve maximum coarsening fine silver in the course of microwave treatment were carried out using silver-containing model samples. The magnetite contents were chosen at 3, 5, 10, and 15%. To confirm the generation of active centers of local heating in the course of microwave treatment of the model samples with the addition of magnetite, heating temperatures were measured over the whole area of the treated samples using a laser pyrometer. Fig. 3 shows the temperature mapping using an example of microwave treatment of a silver-containing model sample with 10% magnetite with sampling points for scanning electron microscopy study. The microwave heating temperature was measured immediately after the treatment. The results of the elemental composition study for the spectra shown in Fig. 3 are presented in Table 5.</p><p>Fig. 3. Temperature mapping of silver-containing model sample at microwave treatment with addition of 10% magnetite with the results of sample examination at selected sampling points using scanning electron microscopy (gray – magnetite; black – model sample)</p><p>Table 5</p><p>The results of the elemental composition study for the spectra presented in Fig. 3</p><p>The interpretation of the obtained data allows confirming arising active centers of local heating in the course of microwave treatment when magnetite was added to the model samples. In Fig. 3, the temperature peaks at the magnetite addition locations, which reach about 600 °C and higher, are clearly visible. At the same time, the heating temperature of the model sample itself is 540–560 °C. The presence of magnetite is confirmed by the results of the elemental composition study.</p><p>The treated silver-containing model samples with magnetite addition were studied using a scanning electron microscope. Figs. 4 and 5 show the results of the study of these samples with magnetite content of 3, 5, 10, and 15%, respectively. The results of the study of elemental composition for the spectra shown in Figs. 4 and 5 are shown in Table 6.</p><p>Fig. 4. Results of scanning electron microscopy study of model samples with coarsened silver after microwave treatment with addition of 3 (left) and 5 (right) % magnetite</p><p>Fig. 5. Results of scanning electron microscopy study of model samples with coarsened silver after microwave treatment with addition of 10 (left) and 15 (right) % magnetite</p><p>Table 6</p><p>The results of the elemental composition study for the spectra presented in Figs. 4 и 5</p><p>The interpretation of the obtained data allows to confirm coarsening fine silver at addition of magnetite as a result of microwave treatment to the particle sizes exceeding the particle size formed in the samples without magnetite, as well as the increase of silver content in the coarsened particles. However, it is worth noting that at a magnetite content of 10%, if compared to the coarsened gold presented earlier in [<xref ref-type="bibr" rid="cit36">36</xref>], spherical-shaped silver particles with an average size of 20–40 μm were found in the silver-containing model samples. This is because the melting point of silver is much lower than that of gold.</p><p>The obtained data on average and maximum sizes of coarsened noble metal particles (aggregates) depending on the magnetite content are presented in Table 7. Besides, Table 7 presents the degree of coarsening measured as the ratio of the average size of the coarsened silver particles to the estimated coarseness of the “invisible” silver.</p><p>Table 7</p><p>Results of the study of the effect of magnetite content on coarsening fine silver in model samples with and without microwave treatment</p><p>Based on the obtained data analysis, it can be concluded that the addition of magnetite, which forms active centers of local heating, contributes to coarsening fine silver particles in the course of microwave treatment, since the treatment of magnetite-free model samples allowed to coarsen the noble metal particles to smaller sizes if compared with the samples with magnetite. The obtained results allow justifying the necessary magnetite content of 10% to achieve maximum coarsening fine silver at microwave exposure to a coarseness of 20–40 μm. The formation of spherical silver particles can be explained by the lower melting point of silver compared to gold.</p></sec><sec><title>3. Treatment of carbonaceous flotation concentrate with addition of substantiated amount of magnetite</title><p>The feasibility of silver coarsening with the addition of the previously substantiated magnetite amount in the course of microwave treatment was investigated on carbonaceous flotation concentrates. In [<xref ref-type="bibr" rid="cit37">37</xref>], the feasibility of coarsening fine Au particles using 10% magnetite at microwave treatment of carbonaceous concentrate was confirmed. Fig. 6 presents the results of a scanning electron microscope study of the treated carbonaceous concentrate, confirming coarsening silver in the course of microwave treatment when added with magnetite in the amount of 10% of the sample weight. The elemental composition of the coarsened particles is presented in Table 8.</p><p>Fig. 6. Results of the study of treated carbonaceous concentrates with addition of 10% magnetite using scanning electron microscopy</p><p>Table 8</p><p>The results of the elemental composition study for the spectra presented in Fig. 6</p><p>The interpretation of the obtained results allows to confirm coarsening silver particles in the course of microwave treatment of carbonaceous flotation concentrate added with 10% magnetite. The size of coarsened particles, which are characterized by spherical shape, after treatment is 20–50 microns. It is worth noting that, besides silver, characteristic peaks of gold were found in the coarsened aggregates according to the results of the study of the elemental composition. This indicates that silver was coarsened together with gold.</p><p>Microwave treatment contributes to increasing the temperature of the model sample, the main part of which is represented by activated carbon. When it is ignited in an oxidizing environment, the following phenomena occur:</p><p>Fig. 7 shows a schematic representation of the mechanism of fine silver coarsening in the course of microwave treatment.</p><p>Fig. 7. Schematic representation of fine silver coarsening in the course of microwave treatment</p><p>Fine silver coarsening is confirmed by the results of scanning electron microscopy examination of the treated silver-containing model samples. In the figures presented in this paper, the coarsened particles are observed both free (not tied with activated carbon and magnetite) and at the initial stage of coarsening directly on the activated carbon surface itself.</p><p>The results of the microwave treatment of carbonaceous flotation concentrate with the addition of 10% magnetite also confirmed the feasibility of fine silver coarsening. The achieved coarseness and the content (grade) of gold and silver in the coarsened spherical particles makes it possible to further extract them and, as a consequence, to reduce losses of valuable components with tailings. Centrifugal concentration can be considered as a potential method for the extraction of the coarsened particles [<xref ref-type="bibr" rid="cit38">38</xref>].</p></sec><sec><title>Conclusion</title><p>The findings of the studies on microwave treatment of silver-containing model samples allowed substantiating the necessity of adding magnetite for fine silver coarsening. Based on the temperature mapping, the formation, in the course of the treatment, of active centers of local heating in the locations of magnetite addition was confirmed. The fine silver coarsening to spherical silver particles, whose average size was 20–40 μm, was achieved at a microwave oven power of 1.0 kW and a treatment time of 3 min with 10% magnetite added. It was revealed that at similar microwave oven power and treatment time of 5 min, with 10% magnetite added, the greatest sizes of coarsened particles containing gold and silver equal to 20–50 μm were achieved. The microwave treatment findings showed that the silver coarsening occurs forming a gravity-extractable form of silver that allowed further investigation of its recovery using gravity concentration methods.</p></sec></body><back><ref-list><title>References</title><ref id="cit1"><label>1</label><citation-alternatives><mixed-citation xml:lang="ru">Федотов П. К., Сенченко А. Е., Федотов К. В., Бурдонов А. Е. 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