Academic literature on the topic 'Purification silicium'

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Journal articles on the topic "Purification silicium"

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Erin, J., D. Morvan, and J. Amouroux. "Rôle de l'hydrogène dans le procédé de purification du silicium par plasma thermique inductif." Journal de Physique III 3, no. 3 (1993): 633–52. http://dx.doi.org/10.1051/jp3:1993154.

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Erin, J., D. Morvan, and J. Amouroux. "Optimisation des conditions de fonctionnement d'un pilote plasma de 25 kW pour la purification du silicium." Journal de Physique III 5, no. 5 (1995): 585–604. http://dx.doi.org/10.1051/jp3:1995148.

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Shablovski, Vladimir, Alla Tuchkoskaya, Vladimir Rukhlya, and Olga Pap. "COAGULANT-FLOCCULANT FROM SECONDARY RESOURCES FOR TREATMENT OF INDUSTRIAL AND MUNICIPAL WASTEWATER." WATER AND WATER PURIFICATION TECHNOLOGIES. SCIENTIFIC AND TECHNICAL NEWS 30, no. 2 (2021): 27–33. http://dx.doi.org/10.20535/2218-930022021240165.

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Coagulants and flocculants are used almost at all drinking water supply facilities, wastewater treatment plants of municipal and industrial enterprises in Belarus and Ukraine to intensify and increase the efficiency of the processes of purification, clarification and discoloration of water and wastewater. Mainly as coagulants aluminum and iron salts are used, as flocculants - active silicic acid, starch, cellulose derivatives, polyacryloamide, etc. 
 Sulfuric acid treatment of alumina-containing raw materials allows, in the course of one process, to obtain a mixture of active substances -
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Starostina, I. V., N. Yu Kiryushina, Е. V. Loktionova, and А. V. Matushkina. "Obtaining a Ferrosilicon Flocculant-Coagulant from Metallurgical Production Waste and Its Usage in Emulsified Wastewaters Purification Process." Ecology and Industry of Russia 26, no. 7 (2022): 20–25. http://dx.doi.org/10.18412/1816-0395-2022-7-20-25.

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A method of obtaining a composite ferrosilicon flocculant-coagulant (FSFC) as a result of acidic modification of slaking steelmaking slag was suggested. It has been determined that the acidic modification of electric-furnace steelmaking slag results in the leaching of basic oxides with the formation of ferric sulfate and silicic acid gel. This allows using the obtained modification product as a ferrosilicon flocculant-coagulant in emulsified wastewaters purification systems. It has been demonstrated that the obtained powdery FSFC at the consumption rate 0.7 g/dm3 provides the emulsion purifica
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Rokosik, E., K. Dwiecki, M. Rudzińska, A. Siger, and K. Polewski. "Column chromatography as a method for minor components removal from rapeseed oil." Grasas y Aceites 70, no. 3 (2019): 316. http://dx.doi.org/10.3989/gya.0709182.

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The purpose of this study was to verify the influence of different chromatographic column beds (silicic acid, activated charcoal, aluminum oxide, silica gel) on the concentration of individual minor components (sterols, tocopherols, carotenoids and chlorophyll) in rapeseed oil. With the use of a combination of these beds, a three-stage optimized method for removing minor components from rapeseed oil was developed. It was demonstrated that the combination of silicic acid and activated charcoal removed about half of the sterols present from the oil. Aluminum oxide turned out to be the most effec
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Lyakhov, Nikolay, Tatiana Grigoreva, Tatiana Talako, Tatyana Udalova, Sergey Vosmerikov, and Evgeniya Devyatkina. "A Carbon-Free Way for Obtaining Nanoscale Silicon." Powders 1, no. 1 (2022): 18–32. http://dx.doi.org/10.3390/powders1010003.

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The nanosized silicon powder has been produced by reduction of silica with magnesium in an argon medium using both the mechanically activated self-propagating high-temperature synthesis and the direct mechanochemical synthesis and has been investigated by X-ray phase analysis, Infrared spectroscopy, electron scanning microscopy, and energy dispersive X-ray spectroscopy. The optimal Mg:SiO2 ratio has been found to provide the minimum content of contaminant impurities of magnesium silicide and silicate in mechanically activated self-propagating high-temperature synthesis. For the first time, dir
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Sathyamoorthy, Neeraja, Nilofer Qureshi, and Kuni Takayama. "Purification and characterization of C28–55 fatty acids from Mycobacterium smegmatis." Canadian Journal of Microbiology 31, no. 3 (1985): 214–19. http://dx.doi.org/10.1139/m85-041.

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The nonmycolic C16 to C55 fatty acids obtained from Mycobacterium smegmatis ATCC 356 by saponification were enriched with respect to the C28 to C55 acids by successive chromatography on silicic acid and Sephadex LH-20 columns. These partially purified fatty acids were then derivatized to the p-bromophenacyl ester and further fractionated by argentation thin-layer chromatography and reverse-phase high-performance liquid chromatography into their individual components.The esters were characterized by electron impact mass spectrometry. Two structural series of C28:1 to C42:1 and C45:2 to C55:2 fa
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Karpychev, E. А. "Determination of sorption characteristics of aluminum hydroxide sludge formed at the stage of pre-purification of water treatment plant." Vestnik IGEU, no. 2 (April 30, 2022): 15–20. http://dx.doi.org/10.17588/2072-2672.2022.2.015-020.

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An urgent task of the research is to describe the properties of the sludge formed during coagulation depending on the type of water supply source. Namely, the aim is to study the sorption capacity of the sludge for the main components removed from the water (iron compounds, organic substances, and silicic acid compounds). This indicator allows you to directly determine the effectiveness of the coagulation. When comparing the actual values of this indicator with practically obtainable values, one can say about the lack or excess of the coagulant supplied for processing. To calculate the specifi
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Liu, Fei, Ling Ke Zeng, Jian Xin Cao, Qian Lin, and Jing Li. "Preparation of Xonotlite Whiskers from Carbide Slag." Key Engineering Materials 434-435 (March 2010): 787–89. http://dx.doi.org/10.4028/www.scientific.net/kem.434-435.787.

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Carbide slag was used as raw materials for the first time to prepare xonontlite whiskers via a hydrothermal route without special instruments and synthesis conditions. And the effect of pH value of emulsion of carbide slag and hydrothermal conditions on removal rate of impurities, morphology and crystallinity of synthesized xonotlite whiskers were explored using ICP, SEM and XRD techniques. The results indicated that the carbide slag after purification could be used to prepare xonotlite whiskers, and different pH values of emulsion of carbide slag had great impact on the removal rate of impuri
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Cho, Young-Sang, Yeonghyun Lee, and Jun Kyu Park. "Fabrication of Silica Microspheres Containing TiO2 or Aluminum Zinc Oxide Nanoparticles via Self-Assembly: Application in Water Purification." Journal of Nanoscience and Nanotechnology 20, no. 11 (2020): 6738–46. http://dx.doi.org/10.1166/jnn.2020.18793.

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In this study, silica micro-particles containing titania (TiO2) or aluminum zinc oxide (AZO) nanopar-ticles were synthesized using emulsion droplets as micro-reactors, for water purification application via photocatalytic decomposition of organic dyes. Towards this end, aqueous silicic acid solution has been emulsified with aqueous dispersion of TiO2 or AZO nanoparticles in a continuous oil phase to form tiny droplets, followed by subsequent self-assembly of the droplets via evaporation. The resulting composite microparticles were controlled to obtain a spherical or porous morphology by adjust
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Dissertations / Theses on the topic "Purification silicium"

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MARONGIU-COMBES, ROS SANA. "Purification des siliciums de type n et p par fusion sous plasma inductif : Rôle du laitier fluore et du potentiel imposé. Application au silicium polycristallin photovoltaique." Paris 6, 1993. http://www.theses.fr/1993PA066420.

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Ce travail a porté sur l'étude des mécanismes de purification du silicium par plasma inductif oxygène en présence d'un laitier fluore sous polarisation. Nous avons focalisé notre travail sur l'élimination du bore et du phosphore qui sont les deux principaux dopants du silicium. La première partie de cette étude a consisté à établir et comparer les diagrammes thermochimiques de stabilité des composés du bore et du phosphore en présence de Baf#2, Caf#2 et Mgf#2. Nous avons conclu qu'en présence de fluor et d'oxygène le bore était éliminé sous forme d'un composé volatil: bof. Nous avons pu déduir
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Abouchi, Hamza. "Purification de silicium solaire dans des réacteurs à grande surface." Thesis, Université Grenoble Alpes, 2020. http://www.theses.fr/2020GRALI035.

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Le silicium de qualité solaire, nécessaire pour approvisionner le marché photovoltaïque en croissance constante, est produit par purification à partir du silicium métallurgique. La voie chimique de purification, la plus classique, a un coût énergétique élevé et pénalités environnementales. La voie métallurgique est une alternative qui doit réduire son coût de production pour répondre au faible prix du marché. Dans ce travail, nous étudions une percée technologique par rapport aux procédés existants pour éliminer le bore, tels que le procédé plasma précédemment étudié dans le laboratoire SIMaP.
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Dégoulange, Julien. "Purification et caracterisation physico-chimique et électriques de silicium d'origine métallurgique destiné à la conversion photovoltaïque." Grenoble INPG, 2008. https://theses.hal.science/tel-00368733.

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L'élaboration de silicium de qualité solaire par une autre route que la voie chimique semble aujourd'hui prometteuse pour réduire les coûts et garantir l'approvisionnement en matériau de la filière photovoltaïque. Un plasma inductif (Ar+H2+O2) couplé à un brassage électromagnétique du silicium liquide permet d'extraire une impureté critique : le bore. La compréhension de la volatilisation du bore a été étudiée via des calculs thermodynamiques sous FACTSAGE ainsi que des analyses chimiques en ligne des gaz de sortie par ICP-OES. L'étude du procédé a été divisée en deux étapes. Le brassage élect
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Vadon, Mathieu. "Extraction de bore par oxydation du silicium liquide pour applications photovoltaïques." Thesis, Université Grenoble Alpes (ComUE), 2017. http://www.theses.fr/2017GREAI067/document.

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L'extraction du bore du silicium liquide est une étape d'une chaîne de procédés de purification de silicium de qualité suffisante pour les applications photovoltaïques. Cette thèse étudie en priorité le procédé dit "gaz froid" qui consiste en l'injection d'un mélange de gaz Ar-H2-H2O sur du silicium liquide chauffé électromagnétiquement. Une deuxième méthode similaire ("procédé plasma") où on injecte un plasma thermique issu d'un mélange Ar-H2-O2 a également été étudiée. Un modèle est nécessaire afin d'optimiser le procédé pour économiser de l'énergie.Les trois objectifs du modèle sont la préd
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Ndzogha, Cyrille. "Etudes des phénomènes d’échange dans la purification du silicium par plasma et induction." Grenoble INPG, 2005. https://theses.hal.science/tel-01340596.

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Ce travail de thèse porte sur un procédé plasma de purification de silicium pour usages photovoltaïque. Il est appliqué à deux types de matériaux : du silicium d’origine métallurgique et des produits de recyclage des boues de sciage des lingots et des plaquettes de la filière photovoltaïque. Les boues de sciage des plaquettes sont essentiellement constituées de liquide de coupe, de particules de SiC (abrasif), de microparticules de silicium et de microparticules de fer provenant du fil de découpe. Le silicium de ces boues est un silicium de haute pureté, qui est déjà de qualité photovoltaïque.
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De, Sousa Matthias. "Contribution à la purification des déchets de silicium solaire oxydé à l'aide d'un procédé assisté par plasma thermique." Thesis, Limoges, 2014. http://www.theses.fr/2014LIMO0033/document.

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La découpe de wafers génère des quantités importantes de déchets de silicium de grade solaire qui ne sont pas revalorisés actuellement à cause de la contamination lors du procédé de découpe. Les travaux présentés dans ce manuscrit portent sur l’étude de la purification de déchets de silicium solaire à l’aide d’un procédé assisté par une torche à plasma d’arc non transféré. Cette étude a été menée selon une double approche numérique et expérimentale. Les calculs numériques ont été réalisés à l’aide d’un code de calcul de mécanique des fluides. Ils sont utilisés pour dimensionner la configuratio
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Rousseau, Sylvain. "Développement du procédé de purification du silicium par plasma thermique RF : mécanisme d’élimination des impuretés : effet simultané de la polarisation électrique du silicium liquide et de la composition du plasma." Paris 6, 2009. http://www.theses.fr/2009PA066547.

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L’objectif de ce travail est le développement d’un procédé de purification du silicium métallurgique par plasma thermique avec polarisation du silicium fondu, dans le but d’augmenter les cinétiques d’élimination des impuretés. Nous avons étudié l’effet simultané de la polarisation et de la composition du plasma sur les processus d’élimination des impuretés. Le suivi en ligne de la purification est effectué par Spectroscopie Optique d’Emission, ce qui permet de comprendre les processus de transfert de matière entre le silicium et le plasma. La composition avant et après traitement des échantill
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Apostolidou, Eleni. "Etude des transferts de chaleur et de matiere lors de la purification du silicium par fusion sous plasma thermique reactif : caracterisation physicochimique du silicium photovoltaique elabore." Paris 6, 1986. http://www.theses.fr/1986PA066173.

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Patatut, Loïc. "Développement d'un dispositif de LIBS pour l'analyse quantitative en ligne des procédés de purification du silicium fondu." Thesis, Université Grenoble Alpes (ComUE), 2015. http://www.theses.fr/2015GREAI100/document.

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L’objectif de ce travail de thèse a été de développer et de valider une méthode d’analyse quantitative du silicium liquide par la technique LIBS (Laser Induced Breakdown Spectroscopy). Pour cela, le dispositif utilisé consiste en une mesure intrusive sur la surface de bulles gazeuses, générées au cœur du métal fondu par soufflage d’un gaz inerte au travers d’un tube. Dans un premier temps, les conditions d’acquisition du signal ont été optimisées pour permettre la répétabilité et la reproductibilité du signal LIBS en dépit des fluctuations paramétriques induites par le bullage. Dans un second
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Apostolidou, Eleni. "Etude des transferts de chaleur et de matière lors de la purification du silicium par fusion sous plasma thermique réactif, caractérisation physico-chimique du silicium photovoltaique élaboré." Grenoble 2 : ANRT, 1986. http://catalogue.bnf.fr/ark:/12148/cb375954878.

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Book chapters on the topic "Purification silicium"

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"are purified lipid contents and others are not, and the puri-(Paspalum scrobiculatum), and barnyard (Echinocloa fied lipid content depends on the purification method. colona). Sridhar and Lakshminarayana [32] also reported Starch lipids (SL) are those bound to starch, and they FL contents of 5.0, 5.6, and 2.2% for Proso, Foxtail, and are the most difficult to extract. Since true SL are present Finger millet, respectively. Taira [45] found slightly high-inside the starch granules, even a very polar solvent such er average FL (ether extraction) contents for glutinous as WSB cannot extract them at ambient temperature. Effi-foxtail millet (4.2-5.1%, average 4.7% of 21 samples) cient extraction of SL requires mixtures of hot aqueous al-than for nonglutinous foxtail millet (4.0-4.7%, average cohol in proportions optimized for controlled swelling of 4.4% of 31 samples). Among millet, pearl millet contains the starch granules and solubilization of the lipids [25]. the most FL. The best solvents are n-propanol or isopropanol with water Lipid contents of rice in Table 2 were cited by Morrison (3:1, by volume) used under nitrogen at 100°C. However, [3] using the data of Nechaev and Sandler [2]. Taira and some n-butanol—water and methanol-water mixtures also Chang [46] reported that the average nonglutinous brown are reasonably efficient extraction solvents at 100°C [25]. rice FL (ether extraction) contents of 20 varieties each of Recently, a third lipid category was introduced. Starch sur-Indica and Japonica types were 2.7% (2.38-2.91%) and face lipids (SSL) are portions of the nonstarch lipids 2.9% (2.54-3.58%), respectively. More recently, Taira et (NSL), which become firmly absorbed onto or into starch al. [47] reported the average FL contents of 15 nongluti-granules during the separation of pure starch [24]. nous varieties as 2.5% (2.24-2.97%) for Indica, 2.5% Lipids are minor components of the cereal grains shown (2.12-2.94%) for Japonica, 2.7% (2.35-3.03%) for Sinica, in Table 2. Data in this table, expressed on a dry basis, and 2.6% (2.11-2.99%) for Japonica types. were calculated from reported values [3,16,26-41]. Also, some BL or TL contents were calculated by subtracting FL from TL or by adding FL to BL, depending on the avail-B. Nonstarch Lipid Classes of Grains ability of data. The FL contents range from 1.5 to 2% of Lipids can be separated into three broad classes by open-the kernel weights of barley, rice, rye, triticale, and wheat column silicic acid chromatography. Nonpolar lipids (NL) grains. They range from 3 to 7% of the kernel weights of are first eluted by chloroform, glycolipids (GL) are eluted oats, millet, corn, and sorghum. However, BL contents in next by acetone, and phospholipids (PL) are eluted last grains are more uniform than FL contents. Therefore, the with methanol. Mixtures of GL and PL are polar lipids FL:BL ratio is substantially higher for corn, millet, oats, (PoL). After NL elution from a silicic acid column, PoL and sorghum than for rye, triticale, and wheat grains. The can be eluted with methanol without the GL elution step. FL:BL ratios for barley and rice are intermediate. Lipids can also be separated into various classes by thin-High oil-containing grains such as corn are continuous-layer chromatography (TLC) using different development ly bred for higher oil content with improved production solvent systems. Each individual lipid class migrates dif-yield. Application of wide-line NMR spectroscopy for ferently on the thin-layer plate, and the difference in mi-nondestructive analysis of the oil content in single corn gration rates makes it possible to separate complex lipids kernels made selection for higher oil content more efficient into classes. The NL consists of SE, TG, DG, MG, and [42]. Corn hybrids with 6-8.5% oil content and grain FFA (see Table 1). The total NL content is obtained by yields equal to those of good commercial hybrids were adding these NL class contents as measured by densitome-produced [43]. try. Thus, the NL content of samples may differ, to some Several kinds of millet exist, and the lipid data in the extent, depending on methodology used (column separa-literature are confusing. Rooney compared the FL (ether tion or TLC separation). extraction) contents of several types of millet in a review The data [1,13,27,29,32,36-38,40,48-58] shown in paper [16]. The average FL contents of pearl millet (Pen-Table 3 may be used for only approximate comparison of nisetum typhoids) were 5.1% (4.1-5.6%, 14 samples), the NL content from different grains because some were 5.4% (2.8-8.0%, 167 samples, [44]), 5.6% (4.3-7.1%, 40 obtained by column chromatography and some by TLC. samples), and 6.2% (4.2-7.4%, 35 samples) [16]. Other All cereal grain lipids are richer in NL than in other class-reported average FL contents were 4.8% (4.6-5.0%, 6 es: 60-70% of the TL are NL in wheat (hexaploid), triti-samples) for foxtail millet (Setaria Italica), 5.8% cale, and rye; 65-80% for barley and oat groats; 77-87% (5.5-6.3%, 6 samples) for Japanese millet (Echinochloa for sorghum and rice; and 75-96% for corn and millet crusgalli), and 4.2% (3.8-4.9%, 20 samples) for proso (Pennisetum americanum). Sridhar and Lakshminarayana millet (Panicum miliaceum) [16]. Sridhar and Lakshmi-[32] reported 82, 80, and 79% of NL for Foxtail, Proso, narayana [30] reported a FL content range of 3.4-5.7% for and Finger millet, respectively. There are significant vari-small millet, including little (Panicum sumatrense), kodo etal effects on the NL/PoL ratio for corn and millet (P." In Handbook of Cereal Science and Technology, Revised and Expanded. CRC Press, 2000. http://dx.doi.org/10.1201/9781420027228-43.

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