Relevant bibliographies by topics / Extraction metallurgy

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  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Extraction metallurgy'

Author: Grafiati
Published: 4 June 2021
Last updated: 6 February 2022

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Journal articles on the topic "Extraction metallurgy"

1

Heimala, Seppo. "Extraction metallurgy." International Journal of Mineral Processing 35, no. 1-2 (June 1992): 147–48. http://dx.doi.org/10.1016/0301-7516(92)90010-t.

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Warner, N. A. "Extraction metallurgy '89." Minerals Engineering 2, no. 3 (January 1989): 437. http://dx.doi.org/10.1016/0892-6875(89)90015-0.

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Barley, R. W. "Extraction Metallurgy '89." Minerals Engineering 2, no. 4 (January 1989): 569–72. http://dx.doi.org/10.1016/0892-6875(89)90091-5.

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Doyle, F. M. "Extraction metallurgy '85." International Journal of Mineral Processing 23, no. 1-2 (May 1988): 157–59. http://dx.doi.org/10.1016/0301-7516(88)90011-7.

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Phillips, C. V. "Extraction metallurgy (3rd edition)." Minerals Engineering 3, no. 3-4 (January 1990): 381. http://dx.doi.org/10.1016/0892-6875(90)90134-w.

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Wilson, A. Matthew, Phillip J. Bailey, Peter A. Tasker, Jennifer R. Turkington, Richard A. Grant, and Jason B. Love. "Solvent extraction: the coordination chemistry behind extractive metallurgy." Chem. Soc. Rev. 43, no. 1 (2014): 123–34. http://dx.doi.org/10.1039/c3cs60275c.

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Jena, P. K., and E. A. Brocchi. "Metal Extraction Through Chlorine Metallurgy." Mineral Processing and Extractive Metallurgy Review 16, no. 4 (1996): 211–37. http://dx.doi.org/10.1080/08827509608914136.

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JENA, P. K., and E. A. BROCCHI. "Metal Extraction Through Chlorine Metallurgy." Mineral Processing and Extractive Metallurgy Review 16, no. 4 (January 1997): 211–37. http://dx.doi.org/10.1080/08827509708914136.

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SHARMA, B. P., and P. K. SINHA. "Extraction and Powder Metallurgy of Beryllium." Mineral Processing and Extractive Metallurgy Review 13, no. 1 (October 1994): 99–112. http://dx.doi.org/10.1080/08827509408914104.

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Wilson, A. Matthew, Phillip J. Bailey, Peter A. Tasker, Jennifer R. Turkington, Richard A. Grant, and Jason B. Love. "ChemInform Abstract: Solvent Extraction: The Coordination Chemistry Behind Extractive Metallurgy." ChemInform 45, no. 15 (March 27, 2014): no. http://dx.doi.org/10.1002/chin.201415289.

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Dissertations / Theses on the topic "Extraction metallurgy"

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Tarkan, Haci Mustafa. "Air-assisted solvent extraction." Thesis, McGill University, 2006. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=102735.

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Air-Assisted Solvent Extraction (AASX) is a novel concept that uses a solvent-coated bubble to contact the organic and aqueous phases. The advantages over conventional solvent extraction (SX) are high solvent to aqueous contact area with reduced solvent volume and ease of phase separation due to the buoyancy imparted by the air core. This opens the way to treat dilute solutions (<1 g/L), such as effluents.
The novel contribution in this thesis is the production of solvent-coated bubbles by exploiting foaming properties of kerosene-based solvents.
The basic set-up is a chamber to generate foam which is injected through a capillary (orifice diameter 2.5 mm) to produce solvent-coated bubbles (ca. 4.4 mm) which release into the aqueous phase. This generates a solvent specific surface area of ca. 3000 cm-1, equivalent to solvent droplets of ca. 20 mum. Demonstrating the process on dilute Cu solutions (down to 25 mg/L), high aqueous/organic ratios (ca. 75:1) and extractions are achieved. The solvent readily disengages to accumulate at the surface of the aqueous solution.
The LIX family of extractants imparts some foaming to kerosene based solvents but D2EHPA does not. An extensive experimental program determined that 1.5 ppm silicone oil provided the necessary foaming action without affecting extraction or stripping efficiency, greatly expanding the range of solvents that can be used in AASX.
To complement the foam study, films on bubbles blown in solvent were examined by interferometry (film thickness) and infra-red spectroscopy (film composition). A "bound" solvent layer was identified with an initial thickness of ca. 2 - 4 mum, comparable to that determined indirectly (by counting bubbles in an AASX trial and measuring solvent consumption). The film composition appeared to be independent of film thickness as it decreased with time.
As a start to scaling up, the single bubble generation system was adapted by installing up to 8 horizontal capillaries. The bubbles generated were ca. 3.4 mm. Trials showed the multi-bubble set up was a simple replication of the individual bubble case. Preliminary analysis of kinetic data shows a fit to a first-order model.
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Langlais, Joseph. "Strontium extraction by aluminothermic reduction." Thesis, McGill University, 1991. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=22447.

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The Melt-Leach-Evaporation (MLE) process is under development for the extraction of valuable Group IA or IIA metals of the Periodic Table, such as lithium, calcium, magnesium and strontium. The process consists of mixing and contacting the value metal source material, which might be an ore or concentrate, with an excess of molten metal which is acting as a reductant and lixiviant. In the process, the value metal extracted from the source material is dissolved in the excess molten metallic solvent and is subsequently extracted as a vapour by vacuum distillation. The vapour is condensed and recuperated in the metallic state.
An experimental program involving eight experiments was carried out. The experimental procedure consisted in essence of melting the aluminum reductant in a crucible and adding the source material, SrCO$ sb3,$ and other reactant (Mg or Bi). (Abstract shortened by UMI.)
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Suriyachat, Duangkamol. "Zirconium solvent extraction using organophosphorus compounds." Thesis, McGill University, 1992. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=60718.

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This study compares zirconium extraction from hydrochloric acid solutions using either Cyanex 923 or Cyanex 925 in kerosene. While both are mixtures of trialkyl phosphine oxides, the trialkyl groups in the former have straight chains, while those in the latter have branched chains.
The major variables studied were hydrochloric acid, extractant and zirconium concentrations, and phase ratio. With both reagents, zirconium is extracted rapidly. Extraction increases with increasing hydrochloric acid concentration, and zirconium is loaded as its neutral tetrachloride complex by a solvation reaction. The loaded zirconium forms a di-solvate, except at high excess extractant concentrations, where solvation numbers greater than 2 are found. At a constant total chloride concentration, the zirconium extraction level is maintained if hydrochloric acid is partially replaced by lithium chloride, provided sufficient hydrochloric acid is retained to prevent zirconium hydrolysis. Distribution coefficients decease with increasing zirconium concentration, suggesting that polymerization occurs in the aqueous phase.
For given conditions, zirconium extraction into Cyanex 923 is higher than for Cyanex 925. However, loading selectivity for zirconium over other metals has not been studied. A few preliminary experiments have shown that aqueous solutions of ammonium carbonate are potential stripping agents.
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Ashrafizadeh, Seyed Nezameddin. "Solvent extraction and liquid membrane separation of rhodium." Thesis, McGill University, 1996. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=37698.

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The aim of this work was to develop a viable solvent-extraction based system for the separation of rhodium (Rh) from aqueous chloride solutions. Ultimately, two different systems were developed. Kelex 100, a commercially available derivative of 8-hydroxyquinoline, was used as the extractant reagent in both of these systems. One of the systems involved the supported liquid membrane (SLM) extraction of Rh. In this system a very thin microporous "Gore-Tex" polymer sheet, impregnated with an organic solution of Kelex 100, served as the SLM. The other system involved the conversion of the chlorocomplexes of Rh to bromocomplexes prior to their solvent extraction with Kelex 100.
The results of the lab-scale experiments using a SLM of Kelex 100 having a surface area of 44 cm2 are reported. The optimum conditions for Rh permeation were found as a feed solution of 2.5 M HCl and a strip solution of 0.1 M HCl. The SLM was quite stable at the optimum conditions with no sign of organic loss or membrane deterioration after 72 hours of operation. It was determined that the HCl activity gradient across the membrane acts as the driving force that "pumps" the non-aquated Rh chlorocomplexes against their concentration gradient. The mechanism of Rh permeation was the ion-pair formation between the protonated Kelex 100 and RhCl6 3- complexes. The rate of Rh permeation was in the order of 10-6 mol.m-2.s-1. The mechanism of HCl and H2O permeation, which were co-extracted along with Rh chlorocomplexes, were found to be the hydration of protons at the low feed acid region and the formation of microemulsions at the high feed acid region. The permeated acid and water were separated from the SLM receiving phase by contacting the latter phase with an organic solution of trioctylamine (TOA). The chlorocomplexes of Rh(III) and acid are readily extracted to the TOA organic phase and subsequently subjected to differential stripping with a concentrated solution of Cl- and a mild NaOH solution, respectively. By interfacing the TOA solvent extraction with the SLM of Kelex 100 highly concentrated solutions of Rh (at least 10 times the initial concentration) and raffinates essentially free of rhodium were produced.
The UV-Visible investigations revealed that the bromocomplexes of Rh undergo aquation to a much lesser extent than that of the chlorocomplexes. The chlorocomplexes of Rh were converted to bromocomplexes by precipitating first the Na(NH4)2Rh(NO2)6 salt and subsequently dissolving that in an HBr solution. The newly formed bromocomplexes of Rh(III) responded very favorably to extraction with Kelex 100. Relatively high distribution coefficients, about 20, and very steep extraction isotherms were generated. The freshly loaded Kelex 100 organic was efficiently stripped upon contact with a strip solution of 6--8 M HCl and a contact time of 10--12 hours. The developed system shows high promise from a practical implementation point of view.
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Parker, N. I. "Contacting schemes for copper extraction." Thesis, University of Bradford, 1987. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.380357.

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Jespersson, Niklas, and Torbjörn Sandberg. "Evaluation of different non-metallic inclusions in steel chips by using electrolytic extraction : Evaluation of a methodology for electrolytic extraction and scanning electron microscopy - energy dispersive spectroscopy (SEM-EDS) analysis." Thesis, KTH, Materialvetenskap, 2021. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-298419.

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Analysing non-metallic inclusions (NMI) by conventional microscopy is prone to errors.  Better imaging can be achieved by using electrolytic extraction (EE) to effectively dissolve the metal matrix, freeing the inclusions so that they can be collected on a filter.  This method of studying NMI was tested on a 157C steel chip, with EE taking place three times on the same surface with increasing levels of  charge  applied.  The  relationship  between  charge  and  extracted  layer depth was examined, so as to facilitate the targeting of NMI from specific depths.  A selection of the extracted inclusions were micrographed with scanning electron microscopy (SEM) and had their compositions measured with energy dispersive spectroscopy (EDS). Based on this data, two methods of classifying NMI were briefly  examined:  manual  classification,  mostly  based  on images,  and  a  semi-automated process based on a sorting algorithm applied to the compositions. The study implies that it is possible to dissolve a 157C steel to a desired depth by applying a charge proportional to it, but the current method introduces an error which might limit the resolution of depth by a significant amount.  Also in the current method, there was no systematic way to select NMI for micrography, and no solution to this problem was found.  The semi-automated classification algorithm  was  compromised  by  inaccurate  readings  of  compositions  from the EDS, and could not be thoroughly tested.
Konventionell  mikroskopi  kan  lätt  ge  felaktig  information  vid  analys  av icke- metalliska  inneslutningar  (NMI),  men  bättre  resultat  kan  uppnås  om  metall- matrisen  löses  upp  med  elektrolytisk  extraktion  (EE),  så  att inneslutningarna frigörs och kan samlas upp på ett filter.  Denna metod att studera NMI testades på ett spån av 157C-stål, med trefaldig EE på samma yta och successivt ökande maximal laddning.  Sambandet mellan laddning och upplöst lagerdjup undersöktes för att möjliggöra extraktion av NMI från givna djup.  Ett urval av de frigjorda inneslutningarna  fotograferades  i  ett  SEM  och  sammansättningarna fastslogs av  EDS.  Dessa  data  låg  till  grund  för  en  undersökning  av  två klassifikationsmetoder  för  NMI:  manuell  klassificering,  till  största  del bildbaserad,  och  en halvautomatisk klassificering där en algoritm sorterar efter sammansättningar. Denna studie antyder att ett 157C-stål kan lösas upp till önskat djup genom  att åläggas en laddning proportionell mot djupet, men den nuvarande metoden introducerar  ett  fel  som  kan  ha  betydande  påverkan  på  noggrannheten.   Den aktuella  metoden  saknar  ett  systematiskt  sätt  att  välja  NMI  för mikroskopfotografi, och ingen lösning har kunnat framföras på detta problem. Den halvautomatiska  klassifikationsalgoritmen  rubbades  av  störningar  i  EDS-resultaten och kunde inte undersökas till fullo.
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Smeets, Alexander Arnoldus Johannes. "Extraction of lithium by vacuum thermal reduction." Thesis, University of Cambridge, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.304440.

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El-Ammouri, Elias G. "Hafnium solvent extraction from chloride solutions using organophosphorus reagents (Cyanex 923, 925)." Thesis, McGill University, 1994. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=69792.

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A comparison of hafnium solvent extraction from hydrochloric acid solutions using either Cyanex 923 or 925 (organic extractants) diluted in kerosene was established. Since understanding of the hafnium-hydrochloric acid solution is important, development of a speciation diagram for such a solution was carried out. While both Cyanex 923 and 925 are mixtures of trialkyl phosphine oxides, the trialkyl group in the former have straight chains, while those in the latter have branched chains.
Experimentally, the major variables studied were hydrochloric acid, hafnium and Cyanex concentrations. Hafnium is rapidly loaded as the tetrachloride complex by a solvation reaction forming a disolvate with the extractant (923 or 925). While extraction increases with increasing acid concentration, it decreases with increasing hafnium concentration due to polymerization. Total chloride level is the controlling factor provided there is enough acid to prevent hafnium hydrolysis and polymerization. Cyanex 923 is a more powerful extractant than Cyanex 925 for given conditions. A few experiments have shown that a very dilute hydrochloric acid solution is suitable as a stripping agent.
The main objective is to evaluate the potential of Cyanex 923 (or 925) as an alternative to MIBK due to the problems associated with the latter. MIBK is the conventional extractant for hafnium and zirconium extraction and separation from hydrochloric acid/thiocyanate solutions. Thus, preliminary studies of hafnium and zirconium (existing separately or together) extraction from hydrochloric acid/thiocyanate solutions were also performed. When existing separately, hafnium and zirconium are similarly extracted into either Cyanex reagents, but when both metals coexist in the same solution, preferential separation of hafnium is observed.
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Mihaylov, Indje O. (Indje Ognianov). "Gallium solvent extraction from sulphate solutions using organophosphoric acid reagents (D2EHPA, OPAP)." Thesis, McGill University, 1991. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=70338.

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The subject of this work is gallium extraction from sulphate solutions--an additional source of this metal from hydrometallurgical zinc production--with organophosphorus acid reagents: di-2-ethyl hexyl phosphoric acid (D2EHPA) and OPAP, a mixed extractant consisting of mono- and di-octyl phenyl phosphoric acids. Extraction proceeds via cation-exchange and Ga$ sp{3+}$ is the reacting species. Gallium is extracted with D2EHPA mostly as GaR$ sb3$ - HR. The results for OPAP suggest existence of four reactions, which form GaM$ sb3,$ GaM$ sb2$D, GaMD$ sb2,$ and GaD$ sb3;$ this explains and allows prediction of behaviour over a wide range of OPAP compositions. Sulphate complexation causes decrease in concentration of the reacting species, and thus lower $D sb{ rm Ga}$ values and extraction rates. Prior knowledge on gallium aqueous complexes is used, and an algorithm developed, to allow quantitative prediction of complexation effects on extraction. The model of mass-transfer with chemical reaction, verified with several known criteria for reaction site determination, describes well the kinetic data for the Ga-D2EHPA system. The model is further developed to account for the stronger acidity and the monomer/dimer equilibria typical for the kind of extractants used. A detailed reaction mechanism is proposed and the first organic ligand addition is found as rate-limiting. The model parameters, estimated from extraction kinetic data, are reasonable, when compared with those obtained for other metals elsewhere. The model's predictions agree with the results from stripping kinetics; the equilibrium conditions (zero rate) can also be satisfactorily predicted, as found by comparisons with the equilibrium data. Ga-D2EHPA and Ga-OPAP systems are compared with an emphasis given to the potential for metal separation; the importance of the ligand exchange rate constant is illustrated with the example of Ga and Al extraction/stripping and their separation based on different rates with
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Benguerel, Elyse. "An investigation on the solvent extraction of rhodium from aqueous chloride solutions /." Thesis, McGill University, 1991. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=61340.

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The aqueous behaviour of rhodium (III) (Rh) in chloride solutions was investigated with the objective of evaluating its response to solvent extraction with 8-hydroxyquinoline derivatives. A theoretical analysis of the abundance of the various chloro-complexes in solution revealed that monoaquo-pentachlororhodate and hexachlororhodate are the most common forms of Rh(III) in chloride solutions ($>$0.5M Cl$ sp{-}$) and that the relative abundance of hexachlororhodate may be lower than was previously reported.
The extraction degree of Rh(III) with 8-hydroxyquinoline derivatives from solutions ranging in acidity from 0.7 to 8.0M and in chloride concentration from 0.7 to 4M was found to follow the calculated abundance of hexachlororhodate (about 5 to 40% in the region investigated). Also, the extraction mechanism was deduced to be ion-pair formation.
The extraction degree of Rh(III) from similar solutions but previously treated with SnCl$ sb2$, was also investigated, and in this case the extraction was quantitative throughout the acidity and chloride concentration ranges tested. Virtual quantitative stripping can be achieved with four five-minute contacts with 1.7M H$ sb2$SO$ sb4$ + 1M Na$ sb2$SO$ sb4$. A preliminary flowsheet for the industrial application of this solvent extraction process for Rh is presented.
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Books on the topic "Extraction metallurgy"

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Extraction metallurgy. 3rd ed. Oxford: Pergamon Press, 1989.

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Vignes, Alain. Extractive metallurgy: Metallurgical reaction processes. London: ISTE, 2011.

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Vignes, Alain. Handbook of extractive metallurgy. London: ISTE, 2010.

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Handbook of extractive metallurgy. London: ISTE, 2010.

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Vignes, Alain. Extractive metallurgy: Thermodynamics and kinetics. London: ISTE, 2011.

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Vignes, Alain. Extractive metallurgy: Processing operations and routes. London: ISTE, 2011.

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J, O'Connor D. Alumina extraction from non bauxtic materials. Düsseldorf: Aluminium-Verlag, 1988.

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H.H. Kellogg International Symposium, Quantitative Description of Metal Extraction Processes (1991 Harriman, N.Y.). H.H. Kellogg international symposium, quantitative description of metal extraction processes: Proceedings of a symposium sponsored by The Minerals, Metals & Materials Society and Henry Krumb School of Mines, Columbia University, held at Harriman, New York, September 4-6, 1991. Warrendale, Pa: TMS, 1991.

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Hansen, Dennis A. Extraction of titanium and iron from ilmenite with fluosilicic acid. [Washington, D.C.?]: U.S. Dept. of the Interior, Bureau of Mines, 1995.

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Hansen, Dennis A. Extraction of titanium and iron from ilmenite with fluosilicic acid. [Washington, D.C.?]: U.S. Dept. of the Interior, Bureau of Mines, 1995.

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Book chapters on the topic "Extraction metallurgy"

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Vignes, Alain. "Hydrometallurgical Extraction Processes." In Extractive Metallurgy 2, 1–86. Hoboken, NJ USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118616932.ch1.

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Vignes, Alain. "Electrometallurgical Extraction Processes." In Extractive Metallurgy 2, 87–116. Hoboken, NJ USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118616932.ch2.

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Vignes, Alain. "Halide Extraction Processes." In Extractive Metallurgy 2, 117–38. Hoboken, NJ USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118616932.ch3.

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Vignes, Alain. "Sulfide Extraction Processes." In Extractive Metallurgy 2, 255–94. Hoboken, NJ USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118616932.ch6.

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Vignes, Alain. "Physical Extraction Operations." In Extractive Metallurgy 3, 1–13. Hoboken, NJ USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118617106.ch1.

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Dutta, Sujay Kumar, and Dharmesh R. Lodhari. "Fundamentals of Nuclear Metallurgy." In Extraction of Nuclear and Non-ferrous Metals, 3–26. Singapore: Springer Singapore, 2017. http://dx.doi.org/10.1007/978-981-10-5172-2_1.

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Jha, Mahesh C. "Extractive Metallurgy of Molybdenum." In Review of Extraction, Processing, Properties & Applications of Reactive Metals, 73–82. Hoboken, NJ, USA: John Wiley & Sons, Inc., 2013. http://dx.doi.org/10.1002/9781118788417.ch2.

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Maljković, D., Z. Lenhard, and M. Balen. "Extraction of Co(II) and Ni(II) with Cyanex 272." In EMC ’91: Non-Ferrous Metallurgy—Present and Future, 175–81. Dordrecht: Springer Netherlands, 1991. http://dx.doi.org/10.1007/978-94-011-3684-6_18.

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Ibana, Don, Simon Assmann, and Marc Steffens. "Advances in the Development of Electrostatic Solvent Extraction for Process Metallurgy." In The Minerals, Metals & Materials Series, 1971–77. Cham: Springer International Publishing, 2018. http://dx.doi.org/10.1007/978-3-319-95022-8_163.

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Gao, Shengxiang, Haodong Zhu, Zhengtao Yu, Xiaoxu He, and Yunlong Li. "A Method to Chinese-Vietnamese Bilingual Metallurgy Term Extraction Based on a Pivot Language." In Big Data, 3–20. Singapore: Springer Singapore, 2018. http://dx.doi.org/10.1007/978-981-13-2922-7_1.

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Conference papers on the topic "Extraction metallurgy"

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Rhamdani, Ahmad Rizky, Latifa Hanum Lalasari, Florentinus Firdiyono, and Syahrul Fatrozi. "Boron extraction from bittern using 1-octanol." In PROCEEDINGS OF THE 3RD INTERNATIONAL SEMINAR ON METALLURGY AND MATERIALS (ISMM2019): Exploring New Innovation in Metallurgy and Materials. AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0001727.

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Royani, Ahmad, Eko Sulistiyono, Agus Budi Prasetiyo, and Rudi Subagja. "Extraction of magnesium from calcined dolomite ore using hydrochloric acid leaching." In PROCEEDINGS OF THE INTERNATIONAL SEMINAR ON METALLURGY AND MATERIALS (ISMM2017): Metallurgy and Advanced Material Technology for Sustainable Development. Author(s), 2018. http://dx.doi.org/10.1063/1.5038299.

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Prasetyo, Erik, Fathan Bahfie, Muhammad Al Muttaqii, Anton Sapto Handoko, and Fajar Nurjaman. "Zinc extraction from electric arc furnace dust using amino acid leaching." In PROCEEDINGS OF THE 3RD INTERNATIONAL SEMINAR ON METALLURGY AND MATERIALS (ISMM2019): Exploring New Innovation in Metallurgy and Materials. AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0002159.

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Prasetyo, E., Y. I. Supriyatna, F. Bahfie, and K. Trinopiawan. "Extraction of thorium from tin slag using acidic roasting and leaching method." In PROCEEDINGS OF THE 3RD INTERNATIONAL SEMINAR ON METALLURGY AND MATERIALS (ISMM2019): Exploring New Innovation in Metallurgy and Materials. AIP Publishing, 2020. http://dx.doi.org/10.1063/5.0002176.

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Das, Subhabrata, Gayathri Natarajan, and Yen-Peng Ting. "Bio-extraction of precious metals from urban solid waste." In PROCEEDINGS OF THE 1ST INTERNATIONAL PROCESS METALLURGY CONFERENCE (IPMC 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4974410.

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Makertihartha, I. G. B. N., Megawati Zunita, Z. Rizki, and P. T. Dharmawijaya. "Solvent extraction of gold using ionic liquid based process." In PROCEEDINGS OF THE 1ST INTERNATIONAL PROCESS METALLURGY CONFERENCE (IPMC 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4974419.

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Makertiharta, I. G. B. N., P. T. Dharmawijaya, M. Zunita, and I. G. Wenten. "Rare earth element enrichment using membrane based solvent extraction." In PROCEEDINGS OF THE 1ST INTERNATIONAL PROCESS METALLURGY CONFERENCE (IPMC 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4974442.

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Natasha, Nadia Chrisayu, and Latifa Hanum Lalasari. "Calcium extraction from brine water and seawater using oxalic acid." In PROCEEDINGS OF THE 1ST INTERNATIONAL PROCESS METALLURGY CONFERENCE (IPMC 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4974443.

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Ibrahim, Najwa, Eltefat Ahmadi, Shaik Abdul Rahman, M. N. Ahmad Fauzi, and Sheikh Abdul Rezan. "Extraction of titanium from low-iron nitrided Malaysian ilmenite by chlorination." In PROCEEDINGS OF THE 1ST INTERNATIONAL PROCESS METALLURGY CONFERENCE (IPMC 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4974426.

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Wulandari, Winny, Tatang Hernas Soerawidjaja, Stephen Joshua, and Hashfi Rijal Isradi. "Extraction of nickel from nickel limonite ore using dissolved gaseous SO2 – air." In PROCEEDINGS OF THE 1ST INTERNATIONAL PROCESS METALLURGY CONFERENCE (IPMC 2016). Author(s), 2017. http://dx.doi.org/10.1063/1.4974445.

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Reports on the topic "Extraction metallurgy"

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Rozelle, Peter L., Thomas J. Tarka, and Ned Mamula. The Application of Current Mineral Processing and Extractive Metallurgy Technologies to Potential Rare Earth Ores in the U.S. Coal Measures: Near-Term Opportunities to Fill Out the U.S. Value Chain. Office of Scientific and Technical Information (OSTI), December 2019. http://dx.doi.org/10.2172/1595955.

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Thesaurus of mineral processing and extractive metallurgy terms. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1985. http://dx.doi.org/10.4095/305030.

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You might also be interested in the extended bibliographies on the topic 'Extraction metallurgy' for particular source types:
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