Elsevier

Electrochimica Acta

Volume 269, 10 April 2018, Pages 714-723
Electrochimica Acta

The electrochemistry and performance of cobalt-based redox couples for thermoelectrochemical cells

https://doi.org/10.1016/j.electacta.2018.03.032Get rights and content

Abstract

Thermoelectrochemical cells are a promising technology for sustainably generating electricity from waste heat. These electrochemical devices directly convert heat into electricity, with a performance governed by the properties of the redox couple, electrolyte and electrode. In this work the influence of the nature of the redox couple on fundamental properties such as the Seebeck coefficient, diffusion coefficient and charge transfer resistance was investigated. Four different cobalt complexes containing the ligands 2-(1H-pyrazol-1-yl)pyridine) (Co2+/3+(py-pz)3), 2-(1H-pyrazol-1-yl)-4-tert-butylpyridine (Co2+/3+(bupy-pz)3), 2,6-di(1H-pyrazol-1-yl)pyridine (Co2+/3+(pz-py-pz)2) and 1,10-phenanthroline (Co2+/3+(phen)3) were examined in a 3:1 dimethyl sulfoxide: 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate mixture. The performance of each redox couple was governed by the ligand properties. The highest Seebeck coefficient was measured for Co2+/3+(py-pz)3 (2.36 mV K−1) which was attributed to a combination of its small radius, bi-denticity and lower degree of aromaticity. This is higher than the previously reported Co(bpy)3 couple. The highest power output was achieved with the Co2+/3+(py-pz)3 redox electrolyte, using platinum electrodes coated with a carbon layer, which gave 36 mW m−2 from a ΔT of 30 C. The power outputs achieved using the different redox couples was highest for those with a high Seebeck coefficient, good electrochemical reversibility and fast ion diffusion. The electrochemical reversibility depends significantly on the nature of the electrode substrate and it is demonstrated that carbon-coated platinum electrodes can be used to improve the electrochemical reversibility of these redox couples.

Introduction

The thermoelectrochemical cell (thermocell) is a device capable of converting waste heat to electricity with no carbon emissions [1]. Sources of sustainable waste heat include geothermal and industrial sources. Interest in the field of thermal energy harvesting has been increasing in recent years, driven by the urgent need to generate more energy from sustainable sources. Semiconductor-based thermoelectric devices are limited to high temperature operation (>200 °C) due to their decreased efficiency at lower temperatures [[2], [3], [4]]. This leaves the lower temperature range of waste heat (<200 °C) under-utilised, presenting an opportunity for the application of liquid-based thermoelectric devices. The increasing research into liquid-based thermocells is also driven by the higher open circuit voltages achievable for these systems, which is in the mV K−1 range as opposed to the μV K−1 range for a typical solid-state thermoelectric devices [2,[5], [6], [7], [8]].

The thermocell is a two electrode system that uses an electrolyte containing a redox couple. When a temperature gradient is applied to the cell, the temperature dependence of the redox reaction generates a potential difference. The cell potential achievable for a given temperature gradient is represented by the Seebeck coefficient (Se) (Eqn (1)) [7]:Se=ΔVΔT=ΔSrcnFwhere, ΔV is the potential difference between the hot and cold electrodes, ΔT is the temperature gradient between the electrodes, ΔSrc is the entropy change associated with the redox reaction, n is the number of electrons involved in the reaction and F is Faraday’s constant [7].

The entropy change of a redox reaction is influenced by factors such as the structural changes that take place in the redox species and the extent of rearrangement of the solvation shell. Until recently, most research into thermocells focussed on aqueous systems, particularly with the ferri/ferrocyanide redox couple that has a Seebeck coefficient of −1.4 mV K−1 [1]. A number of other redox couples have been examined in both aqueous and non-aqueous media including iodide/tri-iodide (I/I3) [[9], [10], [11]], Cu/Cu2+ [12,13], and mixed redox couple systems, such as ferrocene/ferrocenium (Fc/Fc+) and I/I3 [14]. Recently, we reported the Seebeck coefficient of Co2+/3+(bpy)3 in 3-methoxypropionitrile, at 2.19 mV K−1 [8]. The high Seebeck coefficient of this redox couple is attributed to the high-to-low electronic spin state transition for the Co2+/3+ redox couple, which contributes an additional electronic component to the total entropy change [[15], [16], [17]]. There have also been reports in the literature of Seebeck coefficients as high as 7 mV K−1 [18,19] in non-redox active electrolytes. In non-redox active electrolytes, the potential difference occurs via the formation of a concentration gradient due to the different mobility of ions at different temperatures, rather than the entropy change due to a redox reaction. As such, it is important to make the distinction between redox active and non-redox active electrolytes as they have different mechanisms and applications.

At present, the widespread application of thermocells is limited by their relatively low power and conversion efficiency. While recent research into device design and optimisation has led to some significant improvements in cell potential and power outputs [[20], [21], [22]], there is still significant scope for increased understanding and optimisation of the fundamental properties of thermocells and their materials. The investigation of new redox couples with high Seebeck coefficients is a particularly important avenue for improving the performance. Redox couples for thermocell applications should meet three main criteria: high Seebeck coefficients, electrochemical reversibility and electrochemical stability. Cobalt-based redox couples are a promising class of redox couples for this application as they can have higher Seebeck coefficients than other analogous transition metal complexes [16,23,24]. Cobalt complexes with pyridine-pyrazole chelating ligands have been investigated for use in dye-sensitised solar cells, demonstrating good electrochemical stability and reversibility [[24], [25], [26], [27]]. In this work, four cobalt-complexes with different chelating ligands have been investigated as redox couples for thermocells for the first time. The performance of these complexes is compared to that of Co2+/3+(bpy)3, which is the highest performing cobalt complex, tested in the same solvent systems. Thus, the effects of the different ligands on the fundamental properties of the redox couple, such as the Seebeck coefficient, and the corresponding effects of these properties on overall thermocell performance are discussed.

Section snippets

Materials

Cobalt(II) chloride hexahydrate (≥98%, Sigma Aldrich), 1,10-phenathroline (≥98%, Sigma Aldrich), nitrosyl tetrafluoroborate (95%, Sigma Aldrich), dimethyl sulfoxide (DMSO) (purity≥ 99.0%, Sigma Aldrich), 1-ethyl-3-methylimidazolium tris(pentafluoroethyl)trifluorophosphate ([C2mim][eFAP]) (purity ≥ 99.0%, Merck Millipore), lithium bis(trifluoromethanesulfonyl)imide (99.99%), tris(2-(1H-pyrazol-1-yl)-4-tert-butylpyridine)-cobalt(II)/(III) bis(trifluoromethanesulfonyl)imide (Dyesol) and tris(2-(1H

The effect of redox couple structure on the Seebeck coefficient

The structures of the cationic species Co2+(py-pz)3, Co2+(bupy-pz)3, Co2+(pz-py-pz)2, Co2+(phen)3 and Co2+(bpy)3 are shown in Fig. 1(a)–(e), in addition to the structures of the NTf2- anion (Fig. 1(f)) and the [C2mim][eFAP] ionic liquid (Fig. 1(g)). Although ionic liquids offer many advantages over aqueous solvents, such as good thermal stability and low volatility, their relatively high viscosity can limit the mass transport of the redox couple. To overcome this, a mixed solvent system

Conclusions

Four cobalt-based redox couples, Co2+/3+(py-pz)3, Co2+/3+(bupy-pz)3, Co2+/3+(pz-py-pz)2 and Co2+/3+(phen)3, have been investigated for thermal energy harvesting for the first time. The effect of the ligand on the electrochemical properties and thermocell performance, and how this depends on the nature of the electrodes, has been examined. The largest Seebeck coefficient was achieved using the Co2+/3+(py-pz)3 complex, at 2.36 mV K−1. In addition to the large entropy change observed in Co2+/3+

Acknowledgements

The authors acknowledge funding from the Australian Research Council (ARC) through its Centre of Excellence program (CE140100012) and through the Australian Laureate Fellowship scheme for D. R. M. The authors acknowledge the assistance of Mr Vinay Kandangal in calculating the complex radii.

References (41)

  • A. DeBethune et al.

    The temperature coefficients of electrode potentials- the isothermal and thermal coefficients- the standard ionic entropy of electrochemical transport of the hydrogen ion

    J. Electrochem. Soc.

    (1959)
  • T.J. Abraham et al.

    High Seebeck coefficient redox ionic liquid electrolytes for thermal energy harvesting

    Energy Environ. Sci.

    (2013)
  • T.J. Abraham et al.

    Seebeck coefficients in ionic liquids–prospects for thermo-electrochemical cells

    Chemical communications

    (2011)
  • E. Laux et al.

    Aspects of protonic ionic liquid as electrolyte in thermoelectric generators

    J. Electron. Mater.

    (2016)
  • A. Gunawan et al.

    Liquid thermoelectrics: review of recent and limited new data of thermogalvanic cell experiments

    Nanoscale Microscale Thermophys. Eng.

    (2013)
  • E.H.B. Anari et al.

    Substituted ferrocenes and iodine as synergistic thermoelectrochemical heat harvesting redox couples in ionic liquids

    Chem. Commun.

    (2016)
  • E.L. Yee et al.

    Functional dependence upon ligand composition of the reaction entropies for some transition-metal redox couples containing mixed ligands

    Inorg. Chem.

    (1980)
  • E.L. Yee et al.

    A survey of ligand effects upon the reaction entropies of some transition metal redox couples

    J. Am. Chem. Soc.

    (1979)
  • J.T. Hupp et al.

    Solvent, ligand, and ionic charge effects on reaction entropies for simple transition-metal redox couples

    Inorg. Chem.

    (1984)
  • M. Bonetti et al.

    Thermoelectric energy recovery at ionic-liquid/electrode interface

    J. Chem. Phys.

    (2015)
  • Cited by (38)

    • Other technologies

      2023, Power Generation Technologies for Low-Temperature and Distributed Heat
    • Liquid-based electrochemical systems for the conversion of heat to electricity

      2022, Low-Grade Thermal Energy Harvesting: Advances in Materials, Devices, and Emerging Applications
    • Liquid-state thermocells for low-grade heat harvesting

      2022, Low-Grade Thermal Energy Harvesting: Advances in Materials, Devices, and Emerging Applications
    View all citing articles on Scopus
    View full text