Magnesium Synthesis from Magnesium Oxide Using the Solid Oxide Membrane Process

Krishnan, Ajay; Pal, Uday B.; Lu, Xionggang

doi:10.1149/ma2005-01/31/1260

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“…The variation on this process presented here would mitigate these issues by using MgF₂-CaF₂-MgO electrolyte with high MgO solubility ( Krishnan et al, 2005 ; Krishnan, 2006 ), followed by gravity-driven multiple effect thermal system (G-METS) distillation ( Powell, et.al, 2020 ; Telgerafchi et al, 2021 ; Rutherford et al, 2021 ; Espinosa et al, 2022 ; McArthur et al, 2023 ). G-METS can potentially reduce magnesium distillation energy consumption, capital cost, and other operating costs by as much as 90%.…”

Section: Introductionmentioning

confidence: 99%

Magnesium production by molten salt electrolysis with liquid tin cathode and multiple effect distillation

et al. 2023

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Low-cost clean primary production of magnesium metal is important for its use in many applications, from light-weight structural components to energy technologies. This work describes new experiments and cost and emissions analysis for a magnesium metal production process. The process combines molten salt electrolysis of MgO using MgF₂-CaF₂ electrolyte and a reactive liquid tin cathode, with gravity-driven multiple effect thermal system (G-METS) distillation to separate out the magnesium product, and re-use of the tin. Electrolysis experiments with carbon anodes showed current yield above 90%, while a yttria-stabilized zirconia solid oxide membrane (SOM) anode experiment showed 84% current yield. G-METS distillation is an important component of the envisioned process. It can potentially lower costs and energy use considerably compared with conventional magnesium distillation. Techno-economic analysis including detailed mass and energy balances shows that this electrolyte composition could lower costs by utilizing CaO, which is the primary impurity in MgO, as the Hall-Héroult process uses the sodium impurity in alumina. Analysis options include: raw material types (magnesite rock vs. brine or seawater), drying and calcining using electricity vs. natural gas, and carbon vs. SOM anode type. Using SOM inert anodes results in a cost premium around 10%–15%, mostly due to higher electrical energy usage resulting from membrane resistance, and reduces GHG emissions by approximately 1 kg CO₂/kg Mg product. Capital and operating cost estimates, and cradle to gate greenhouse gas (GHG) emissions analysis under several raw material and process technology scenarios, show comparable costs and emissions to those of aluminum production.

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