2017
DOI: 10.1149/2.f05172if
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Electrochemical Engineering for Commodity Metals Extraction

Abstract: The planet consumes commodity metals such as iron, aluminum, and copper at an unprecedented rate, as the basis for infrastructure, transportation, power generation, or consumer electronics. A review of the existing paradigm in the primary production of those metals is proposed, in particular with respect to energy consumption, productivity, and environmental impacts. Using an analogy with the electrochemical production of liquid aluminum, a discussion of the electrochemical engineering challenges faced to tran… Show more

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Cited by 14 publications
(6 citation statements)
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“…Reaction (5) minimum decomposition voltage is 0.41 V, with actual measurement at 50 A scale of about 5 V (though this has not yet been optimized) [47]. With a cautious estimated faradaic efficiency at 50%, the energy consumption per tonne of Cu is estimated at 4220 kWh, which is comparable with the overall energy consumption in existing smelting [48].…”
Section: Discussion: Towards a Fully Electrified Stepmentioning
confidence: 98%
See 1 more Smart Citation
“…Reaction (5) minimum decomposition voltage is 0.41 V, with actual measurement at 50 A scale of about 5 V (though this has not yet been optimized) [47]. With a cautious estimated faradaic efficiency at 50%, the energy consumption per tonne of Cu is estimated at 4220 kWh, which is comparable with the overall energy consumption in existing smelting [48].…”
Section: Discussion: Towards a Fully Electrified Stepmentioning
confidence: 98%
“…While a full economic evaluation is outside the scope of this paper, the conversion costs of copper in the incumbent smelting-converting-electrorefining route can be used as a benchmark to derive key engineering metrics a new process based on direct electrochemical decomposition must achieve. This method and the corresponding targets are found in a prior work by Allanore [48]. For the conversion costs of an electrolytic process for copper extraction to be on par with the incumbent processes, electricity consumption use must be around 3900 kWh/t.…”
Section: Economic Feasibilitymentioning
confidence: 99%
“…Alternatively, chlorides have high electrical conductivity and are often used as electrolytes in electrowinning and electrorefining. They are disadvantageous insofar as the solubility of oxygen ions is low for oxide electrolysis [13]. On the other hand, the oxide feedstock is highly soluble in the molten oxide, and current density is high due to the high concentration of ions in the electrolyte [14].…”
Section: Introductionmentioning
confidence: 99%
“…The T red ML model thus does not capture the underlying thermodynamics correctly and would not predict useful free energies at temperatures other than the oxide reduction temperature. Hence, the T red ML model does not provide reliable predictions of the temperature-dependent reduction free energy and would therefore not be useful for, e.g., the prediction of reduction potentials for high-temperature electrolysis 31 .…”
Section: Introductionmentioning
confidence: 99%