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The thermoelectrochemistry of the aqueous iron( ii )/iron( iii ) redox couple: significance of the anion and pH in thermogalvanic thermal-to-electrical energy conversion

Thermogalvanic conversion of temperature gradients into electricity via a redox couple represents a potential method of waste energy harvesting, but inexpensive, effective and sustainable redox couples are required. In this study four aqueous Fe( ii )/Fe( iii ) salt systems are considered, based upo...

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Bibliographic Details
Published in:Sustainable energy & fuels 2018, Vol.2 (12), p.2717-2726
Main Authors: Buckingham, Mark A., Marken, Frank, Aldous, Leigh
Format: Article
Language:English
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Summary:Thermogalvanic conversion of temperature gradients into electricity via a redox couple represents a potential method of waste energy harvesting, but inexpensive, effective and sustainable redox couples are required. In this study four aqueous Fe( ii )/Fe( iii ) salt systems are considered, based upon ammonium iron sulphate, iron sulphate, iron trifluoromethanesulfonate and iron nitrate. A range of Seebeck coefficients were observed, from +0.18 ± 0.04 mV K −1 for ammonium iron( ii / iii ) sulphate to +1.46 ± 0.02 mV K −1 for acidified iron( ii / iii ) trifluoromethanesulfonate, both at a temperature difference of 20 K; notably these apparent Seebeck coefficients vary with temperature difference due to significant chemical equilibria. The iron( ii / iii ) nitrate system generated the highest thermogalvanic power output. The systems were probed by cyclic voltammetry, pH, UV-Vis spectroscopy and electrochemical impedance spectroscopy, and two competing mechanisms noted, which strongly affect both the current output and Seebeck coefficient ( i.e. potential output) of their thermoelectrochemical cells (or thermocells). Green and economic consideration are important aspects if these systems are to be employed in harvesting low-grade heat energy at a larger scale; iron nitrate and acidified iron sulphate were the most highly competitive systems.
ISSN:2398-4902
2398-4902
DOI:10.1039/C8SE00416A