Fundamental Differences between Magnesium and Alkali Metal Electrowinning

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In the Kroll and Hunter processes to produce titanium from TiCl4, magnesium and sodium are used respectively as reducing agents. These processes are slow and very energy intensive and consequently much work was done over the years to improve the economics of producing these metals. In this regard, more success has been achieved with improving the economics of magnesium electrowinning than with alkali metal electrowinning. Magnesium electrowinning cells generally have electrodes with a planar shape and alkali metal electrolysis cells have electrodes with a cylindrical shape. Furthermore, recent advances in magnesium electrolysis allowed the introduction of bipolar electrodes, whereas such electrodes have not been introduced in alkali metal electrowinning cells. It is conceptually possible to replicate the advances in the construction of magnesium electrowinning cells to improve sodium or other alkali metal electrowinning cells. However, there are underlying fundamental reasons why it would be difficult to do so.In this paper the technologies for magnesium and alkali metal electrowinning cells are briefly reviewed. The reasons why it would be difficult to copy the improvements made in magnesium electrowinning technology to alkali metal electrowinning technology are then explained in terms of the implications of the underlying chemical and physical properties of the chemicals involved in the processes.

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160-168

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October 2014

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© 2014 Trans Tech Publications Ltd. All Rights Reserved

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[1] Electrolytic cells, Magnesium Encyclopedia, magnesium. com online resource, http: /www. magnesium. com/w3/data-bank/article. php?mgw=81&magnesium=67, Downloaded 1 May (2011).

Google Scholar

[2] K. Grjotheim, H. Kvande, L. Qingfeng and Q. Zhuxian, Metal Production by Molten Salt Electrolysis – Especially Aluminium and Magnesium, China University of Mining and Technology Press, July, (1988).

Google Scholar

[3] J.C. Downs, Electrolytic process and cell, US Patent 1, 501, 756, 15 Jul. (1924).

Google Scholar

[4] O.G. Sivilotti, Metal production by electrolysis of a molten electrolyte, US Patent 4, 514, 269, 30 Apr. (1985).

Google Scholar

[5] E.I. Du Pont De Nemours & Company, Improvements in or relating to the electrolytic production of sodium, British Patent GB 885, 980, 3 Jan. (1962).

Google Scholar

[6] V.J. Reilly, Fused salt electrolysis cell having anode with tapered well therein, US Patent 3, 544, 444, 1 Dec. (1970).

Google Scholar

[7] E.I. Adaev, A.V. Blinov, G.M. Kamarian, V.A. Novoselov, V.N. Suchkov and L.M. Yakimenko, Electrolytic cell, US Patent 3, 507, 768, 21 Apr. (1970).

Google Scholar

[8] H.M. Blank, O.R. Bergmann and W.J. Simmons, Fused chloride salt electrolysis cell, US Patent 5, 904, 821, 18 May (1999).

Google Scholar

[9] Kh. L. Strelets, Electrolytic Production of Magnesium, Translated from Russian by J. Schmorak, Israel Program for Scientific Translations, Jerusalem, (1977).

Google Scholar

[10] C.L. Mantell, Electrochemical Engineering, McGraw-Hill Book Company, (1960).

Google Scholar

[11] G.T. Motock, Electrolysis of lithium chloride in the 1000-Amperes cell, Electrochemical Technology, Mar-Apr. 1963, 122-127.

Google Scholar

[12] G.N. Kannan and P.S. Desikan, Current trends towards energy reduction in electrolytic magnesium production, Bulletin of Electrochemistry, 6 (9) Sept. 1990, 776-779.

Google Scholar

[13] H. Eklund, P.H. Engseth, B.L. Langseth, T. Mellerud and O. Wallevik, Magnesium Technology 2000, Edited by H.I. Kaplan, TMS, (2002).

DOI: 10.1002/9781118859803.ch23

Google Scholar