Thermo-electrochemical cells for harvesting waste heat: Comparison
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Please note this is a comparison between Version 3 by Sirius Huang and Version 2 by Rita Khanna.

Thermo-electrochemical cells (also known as thermocells; TECs) represent a promising technology for harvesting and exploiting low grade waste heat (< 100-150ºC) ubiquitous in the modern environment. Based on temperature dependent redox reactions and ion diffusion, emerging liquid-state thermocells convert waste heat energy into electrical energy generating power at low costs, minimal material consumption and negligible carbon foot-print. Recent developments in thermocell performances are reviewed in this article with specific focus on new redox couples, electrolyte optimisation towards enhancing power output and operating temperature regime, use of carbon & other nanomaterials for producing electrodes with high surface area for increasing current density and device performance. Highest values of output power and cell potentials have been achieved for the redox ferri/ferrocyanide system and Co2+/3+, with great opportunities for further development in both aqueous and non-aqueous solvents. New thermoelectric applications in the field include wearable and portable electronic devices in the health and performance monitoring sectors; using body heat as a continuous energy source, thermoelectrics are being employed for long-term, continuous powering of these devices. Energy storage in the form of micro supercapacitors and in lithium ion batteries is another emerging application. Current thermocells still face challenges of low power density, conversion efficiency and stability issues. For waste heat conversion (WHC) to partially replace fossil fuels as an alternative energy source, power generation needs to be commercially viable and cost-effective. Achieving greater power density and operations at higher temperatures will require extensive research and significant developments in the field.

  • Thermo-electrochemical cells
  • energy harvesters
  • low grade waste heat
  • wearable electronics
  • micro supercapacitors
  • thermoelectrics

[1]1. Introduction

The conversion of energy from primary energy sources to their final use is accompanied by several losses in the form of waste heats. Forman et al. [1] have estimated the waste heat potential in transport, commercial, industrial and residential sectors. Nearly 72% of the primary energy consumed was found to be lost as waste heat, of which ~63% of waste heat streams occurred at temperatures below 100º °C. In the USA, conventional industries and power plants are known to annually waste over 8,000 TWh as low-grade heat [2]. This ubiquitous waste heat energy in the form of vehicle exhaust, industrial  waste heat, geothermal heat, body heat etc., etc., is found distributed almost everywhere. However, vast amounts of low-grade heat areis mostly discarded and rarely exploited commercially due to theirits intrinsic low temperatures, space-time variations and the lack of cost-effective and efficient energy -recovery technologies [3]. Renewable energies such as solar, wind, or nuclear etc., which have a negligible carbon foot-print asprint compared to non-renewable fossil fuels, [4] are seeing a great resurgence.

The transformation of thermal gradients into electrode potentials for generating electricity has been investigated for a long time [5]. The generation of electric potential in the presence of a temperature gradient between different electrical conductors/or semiconductors was discovered by Thomas Johann Seebeck in 1821. Seebeck coefficients, representing the potential difference generated per unit temperature difference, are typically in the order of few µV/K for devices based on semiconductor materials [6]. Early research was mainly in the field of solid-state thermoelectrics ‘thermoelectric generators (TEG)’s) consisting of n- and p- type semiconductors connected in series as modules and then connecting a number of modules in parallel between the heat source and a cold sink. Under the influence of thermal gradients, mobile charge carriers ‘electrons/holes’ diffused from the hot electrode to the cold, building up charges and a small potential difference [7]. 

Early studies, twhichat later led to the thermo rmoelectrochemical converters, were used for applying thermal corrections to electrochemical processes in the field of current sources and in the production of galvanic coatings. However, the gradual dissolution of anodes was found to limit their commercial application [8]. Landry [9] suggested the integration of low- and high -temperature processes to minimize heat losses. Wakao and Nozo [10] developed a process for recovering thermal energy from low-level heat generated during the mixing of nitric acid with water.  The advent of nano-structured thermoelectrics has led to a great deal of interest in waste -heat conversion (WHC) to electricity [11]. Although early research was dominated by thermoelectrics, a number of articles have been published in leading journals on new types of WHC devices using a wide range of phenomena. These include:  thermomagnetic generators [12], ionic heat -to -electricity conversion [13], thermo-osmotic systems [2], liquid-state thermocells [14], high temperature pyroelectric systems [15,16],[15][16] and organic Rankin cycles [17] [17] for applications in industries, construction, transportation, and energy sectors. These devices are used for harvesting energy from a heat sources such as automotive exhaust systems [18], fuel cells [19] [19],or hypersonic engines [20] etc[20]. Such energy harvesting can reduce the charging requirements on batteries while eliminating wired power connections. Most R&D in this field is focussed on developing better n-type and p-type thermoelectric materials.

Thermoelectrochemical (TEC) cells or ‘thermocells’ isare an alternative device design based on redox-active electrolytes which can produce much higher potential differences (mV/K vs. µV/K for solid-state semiconductor devices).  A thermocell has two identical electrodes in contact with a redox couple electrolyte in the cell and an external connection [21]. Under a thermal gradient, the redox reaction causes the oxidation of the redox couple at the anode and reduction at the cathode. The reduced species are transported back to the anode through diffusion, convection and migration in the electrolyte, creating a continuous reaction and current flow. Within the degradation constraints of cell materials, thermocells are capable of continuously generating electricity without consuming materials or producing emissions.

A significant step in the development of thermo-electrochemical systems was the study of TEC cells based on inert electrodes, where the reactions at the electrodes occurred with the release of gaseous products (HNO

3 → NO, N

 → NO, N

2

O

4 and HNO

 and HNO

2

; Br

2 → Br-); the released volatile products later condensed at the counter electrode as the reverse reaction [22–23]. Representative examples of such thermocells are shown in

 → Br−); the released volatile products later condensed at the counter electrode as the reverse reaction [22][23][24]. Representative examples of such thermocells are shown in 

Fig.ure 1. 

. 

Fig.ure 1

a shows a KBr/Br

2 based TEC cell, where the intercalation of Br

-based TEC cell, where the intercalation of Br

2 gas into graphite electrodes plays a key role in the cell operation. At the cold electrode (cathode), Br

 gas into graphite electrodes plays a key role in the cell operation. At the cold electrode (cathode), Br

2 intercalates into graphite, picks up electrons and dissociates into Br- ions. These ions diffuse through the bridge to the hot electrode (anode) and transform into Br

 intercalates into graphite, picks up electrons and dissociates into Br− ions. These ions diffuse through the bridge to the hot electrode (anode) and transform into Br

2 gas releasing 2e-. These electrons travel from the anode to the cathode in the outer loop completing the circuit.

 gas, releasing 2e−. These electrons travel from the anode to the cathode in the outer loop, completing the circuit. 

Fig.ure 1b shows a cell based on organic acetone-iso-propanol thermocouple. Reaction at the anode involves: CH

b shows a cell based on an organic acetone-iso-propanol thermocouple. Reaction at the anode involves CH

3

-CH(OH)-CH

3®CH

 ⟶ CH

3

-C(O)-CH

3 +H

 + H

2 +2e-, and a reverse reaction occurs at the cathode. Such processes allow relatively long and continuous generation of potential difference and provide higher output power values. However, these systems were unstable, and their operation is accompanied by the release of toxic products such as bromine, hydrogen or nitrogen oxides.

 + 2e−, and the reverse reaction occurs at the cathode. Such processes allow the relatively long and continuous generation of potential difference and provide higher output power values. However, these systems are unstable, and their operation is accompanied by the release of toxic products such as bromine, hydrogen or nitrogen oxides.

 

Fig.ure 1: Schematic representations: (a) KBr/Br

. Schematic representations: (a) KBr/Br

2

-based TEC cell, (b) acetone-isopropanol thermocell, (c) Cu

2+

/Cu system in CuSO

4 solution wit

 solution with soluble electrodes, (d) a ferrite/ferrocyanide redox couple ([Fe (CN)6]3−/[Fe (CN)6]4−) with inert electrodes.

The soluble electrodes, (d) a ferrite/ferrocyanide redox couple ([Fe (CN)6]3-/ [Fe (CN)6]4-) wifollowing secth inert electrodes.

Ion this article, we present an in-depth overview on the advances made in TEC design and performances focusing of different aspects, new growth areas and emerging concepts in the choice of redox couples, electrolytes, electrode design and configurations. The article is organized as follows. A brief summary of historical developments in the field is provided in Section 2. Sections 3 and 4 highlight developments in redox couples, electrolytes and electrodes spanning several research directions. Emerging applications of thermocells in the fields of wearable and portable devices, energy storage and associated applications are presented in Section 5. The article concludes with highlighting economic concerns and future perspectives.

2. Historical Background

Some of the early -generation TEC cells involved the gradual dissolution of electrodes, limiting their long -term prospects. One such example is shown in  Fig.ure 1c, consisting of soluble metal (Cu) electrodes placed in CuSO4  solution at two different temperatures. Such a cell will work untill there is a certain degree of electrode consumption, then require a reversal of the temperature gradient for operating in the opposite direction. A significant development was the use of inert electrodes, providing surfaces for released gaseous products such as NO/N2O4/HNO2  or Br-−; the released volatile products were condensed at the counter electrode, where the reverse reaction occurred [24][23][25]. While such processes permitted relatively long and continuous generation of the potential difference as well as higher output power values, these systems had limited stability along with the continuous release of noxious gases. The next stage involved the utilization of redox electrolytes, providing relatively fast kinetics of the electrode process and high values of the hypothetical Seebeck coefficient. Systems based on potassium hexacyanoferrates/ferrites were the most widespread [25][26]; a schematic representation of this cell is given in  Fig.ure 1d. As this system has a negative Seebeck coefficient (-−1.4 mV/K), oxidation takes place at the hot electrode and reduction at the cold electrode. At the hot electrode, Fe (CN)64- − loses an electron and transforms into Fe (CN)63- − which diffuses back towards the cold electrode. At the cold electrode, Fe (CN)63- − picks up an electron to transform into Fe(CN)64-−, which then diffuses towards the hot electrode thereby setting up a perpetual motion of ions and the generation of electric current. It can be seen that the electrodes remained inert during the process and were not consumed. There has been a significant progress in the cell design and yields since early studies on this system.

Several other types of thermoelectric cells have been developed. These are briefly listed below:

  • TEC cells with phase transitions during mass transfer have been studied for a relatively long time (the first publications date back to the 1970s), but these have not found practical application due to their complexity of design and rapid degradation of components. Wang et al. [27] have recently developed electrochemical sodium heat engines based on phase-change reactions. Nevertheless, their important advantage is their continuous operation, which does not require changing hot and cold sources.
  • Typical TECs are non-isothermal electrochemical cell systems consisting of two electrodes, an electrolyte and a separator. The conversion of thermal energy into electrical energy involves electrode kinetics, thermodynamics, and heat and mass transfer. TEC cells involve changes in the aggregate state of oxidized and reduced forms (nitric acid and nitrogen oxides or KBr and Br2) during continuous operation [8][28].
  • Thermally regenerative electrochemical cycles (TREC) consist of two electrodes with opposite thermopowers; anodes and cathodes generally have positive and negative thermopowers, respectively. For negative thermopower, the cycle involves cooling, discharging, heating and charging; for positive thermopower, the cycle involves heating, charging, cooling and discharging [29].
  • Other cell configurations include thermogalvanic cells (TGC) based on soluble, reversible metal electrodes in solutions of their own salts at different temperatures—TECC cells, using inert electrodes placed in a redox electrolyte or ionic liquid; TGC-Li cells, based on a Li+/Li redox system; TRABs (thermally regenerative ammonia-based batteries); DTCCs (direct thermal charging cells); etc. [30][31][32][33].
  1. TEC cells with phase transitions during mass transfer have been studied for a relatively long time (first publications dating back to the 1970s), but these have not found practical application due to the complexity of design and rapid degradation of components. Wang et al. [26] have recently developed electrochemical sodium heat engines based on phase change reactions. Nevertheless, their important advantage is the continuous operation, which does not require changing hot and cold sources.
  2. Typical TECs are non-isothermal electrochemical cell systems consisting of two electrodes, electrolyte and a separator. The conversion of thermal energy into electrical energy involves electrode kinetics, thermodynamics, heat and mass transfer. TEC cells involve changes in the aggregate state of oxidized and reduced forms (nitric acid and nitrogen oxides or KBr and Br2) during continuous operation.
  3. Thermally regenerative electrochemical cycles (TREC) consist of two electrodes with opposite thermopowers; anodes and cathodes generally have positive and negative thermopowers respectively. For negative thermopower, the cycle involves cooling, discharging, heating and charging; for positive thermopower, the cycle involves heating, charging, cooling and discharging [27].
  4. Other cell configurations include thermogalvanic cells (TGC) based on soluble, reversible metal electrodes in solutions of their own salts at different temperatures; TECC cells use inert electrodes placed in a redox electrolyte or ionic liquid; TGC-Li cells based on Li+/Li redox system; TRABs (thermally regenerative ammonia-based batteries), DTCCs (direct thermal charging cells) etc. [28-31].

 

3. Electrode mMaterials and dDesign

Due to their non-reactive and thermally stable nature, platinum electrodes were used during early studies on thermocells. The electrolyte had to be stirred continuously to achieve Carnot efficiencies of 1.2% [32][34]. High power generation in thermocells requires large current densities, which may be achieved through high concentrations of redox mediators, increasing the number of sites for redox reactions and exposing electrodes to large thermal gradients [35]. Different types of thermocell electrodes and materials are detailed next.

Reversible metal electrodes:  Thermocells using ‘reversible electrodes’ consist of soluble metal electrodes placed in solutions of corresponding salts at two different temperatures (Fig.ure 1Cc). This cell can only work untill a certain level of electrode consumption, is reached; the direction of the temperature gradient is then reversed for the cell to work in the opposite direction. Most of the studies have been reported on the Cu2+/Cu system due to its simple design and good reproducibility. Seebeck coefficients for this system could be modified from hypothetical values of 0.879 mV/K to 0.75 - –1.32 mV/K by changing experimental conditions and electrolyte additives [33][36]. Natural convection was found to have a significant influence on the efficiency of Cu/Cu2+-based thermogalvanic cells. Burmistrov et al. [34][37] have reported on the efficiency of thermocells based on copper, zinc and nickel metallic electrodes. While the efficiency parameters for Cu electrodes agreed well with the theoretical data and published results, the efficiency of zinc-based TEC cells was somewhat lower than found to be theoretical expectations. The thermogalvanic system with nickel electrodes in an aqueous solution of nickel sulfphate exhibited an unusual behaviour. 

Inert carbon electrodes:  Carbon-based electrodes are becoming increasingly important as a promising and affordable alternative to platinum electrodes. Nanostructured carbon materials, such as single (SWNT) and multiwalled carbon nanotubes (MWNT), and graphene etc.e, have a large surface area, thatwhich helps in increasing the number of reaction sites. Depending on the number of nanotube walls, the specific surface area of CNTs lies in the range 50–1315 m2/g [35][38]. These materials also show fast electron -transfer kinetics for the ferrite/ferrocyanide redox couple. Both of these properties can increase the current density achieved with the thermocouple [36][39].

Hollow nickel microspheres electrodes:  Burmistrov et al. [37][40] have shown that hollow Ni microspheres can be an effective electrode material for thermoelectrochemical cells and provide extremely high values of the hypothetical Seebeck coefficient and open circuit voltage. Electrodes were prepared by pressing tablets of nickel microspheres and reduced at 250 °C. MThe most effective composition of KOH , a KOH-based alkaline electrolyte, was chosen based on the influence of the alkali content on the hypothetical Seebeck coefficient value and specific power as determined by the number of charge carriers in the electrolyte and the intensity of reactions at the electrodes [38][41][42].

 

4. Emerging Applications

The conversion of waste heat to electrical energy is finding application in several fields. Some of the emerging applications are presented in this section. While some of these are stand alone on TE effect, others are in conjunction with other technologies.

Wearable and portable devices:  Wearable electronic devices are gaining attention in the health and performance -monitoring sectors towards long-term, continuous, self-powered operations using hthe human body as a continuous supply of energy. HThe harvesting of body heat in wearable devices has been investigated extensively as an alternative to bulky batteries that require frequent charging or replacement [39, 40] [43][44]. As the core body temperature is regulated at 37 °C, body heat can be a continuous source of energy; the total heat dissipated from the human body can range between 60 to 180 W depending on the activity level [41][45]. As only a small fraction of the body’s surface can be covered by TEG devices, overall efficiencies are likely to be quite small. Of the several approaches used for harvesting body heat such as electrostatic, piezoelectric, electromagnetic, pyroelectric and thermoelectric effects, we will the focus our attentionwill be on thermoelectric mechanisms [42][46]. Wearable electronic devices find application in medical devices (real -time monitoring, blood pressure sensors, ear-ware), smart watches, sportswear, wristbands, and flexible devices for monitoring non-flat surfaces in industrial applications [43][47].

In rigid TEGs, n- and p-legs and interconnects are typically affixed to a thermally conductive ceramic substrate (alumina or aluminium nitride). In flexible TEGs, Ggallium-Iindium eutectic alloys have been used as flexible liquid-–metal interconnects to ascertain integrity during operation; Kapton HN and polydimethylsiloxane are the two most common substrates [44][48]. Typical power outputs are found to range between 2 to 8.75 µW/cm2 [45] [49]. Liu et al. [46][50] have presented several different designs for wearable devices for harvesting body heat in a range of applications.

Energy storage devices:  The integration of energy-harvesting and storage devices has been extensively investigated for emerging self-powered electronic devices [51]. Thermoelectric generators can be used to convert excess heat generated during the operation of electronic devices into electricity [52].  Using the Soret effect, ionic thermoelectric supercapacitors utilize ionic electrolytes to produce charges and energy storage in a single device; the operation of these devices is, however, limited by long charging and discharging times and a rigid configuration [47][53][54]. Yang et al. [48][55] have reported on a TEG  device with n- and p- type modules consisting of Ag2Te- and Ag2Se -nanoparticle thin films. This device was directly linked with a planar micro supercapacitor. A Seebeck voltage of 82 mV was generated for DT ΔT of 15.8 K and a charging efficiency of 98%.

Park et al. [49][56] have reported an all-in-one energy system consisting of a TEG on one side of the substrate and a micro supercapacitor (MSC) on the other side. The TEG was constructed from screen -printed p- and n- modules and a p- type TE film for alignment with electrodes. An MSC was fabricated on the other side using rGO/CNT electrodes and Au current collectors. Electrodes were positioned above and below the TEG-substrate-MSC system; the electrode on the TEG side was connected externally to the current collector of MSC. This system was able to generate 10.8 V of electrical energy for thermal differences up to 10 K and store it without loss.

5. Conclusions and fFuture pPerspectives

Development of thermoelectrochemical technologies for harvesting waste low-temperature heat opens the prospect of increasing the efficiency of various devices and mechanisms operating in exothermic mode or creating systems for generating electricity based on natural heat sources. Any process that can partially replace fossil fuels as a prime energy source will be used only if it is attractive to industry; an alternative energy source such as waste heat conversion (WHC) has to cost effective to becoming commercially viable. Geoffroy et al. [50][57] have shown that current WHC heat engines are not economically viable below 100ºC and require temperatures above 150ºC coupled with 100-1000 kW power outputs to be economically competitive. Studies in recent years have shown the possibility of significant increases in the power and conversion efficiency of TEC cells. Highest values of output power and cell potentials have been achieved for the redox ferri/ferrocyanide system and Co2+/3+, which offers great opportunities for further development and research in both aqueous and non-aqueous solvents.

Achieved results show the pathways to overcome key fundamental limitations of thermocell performance and set new tasks for fundamental research and further development of electrodes, electrolyte materials and cell design. One of the key tasks in thermocells development is to investigate mechanisms of entropy change via new redox couples and electrolytes. This will be related to increasing the hypothetical Seebeck coefficient, as well as improving the properties of electrodes and solvents to increase the mass transfer rate (diffusion capacity) towards increasing exchange currents and output power values.

One of the most promising thermoelectric power generation application involves vehicle waste heat recovery to improve fuel economy, wherein waste heat from the exhaust, is redirected to produce electricity. Other applications include harvesting industrial waste heat (incinerators, cement, steel mills etc.), geothermal, fuel oil-fired furnaces or gas water-heaters with this technology. Despite extensive research, WHC technology has yet to achieve significant market penetration. For WHCs to become be a serious contender, it has to compete with solar, wind, geothermal technologies in terms of capacity factors, capital costs, operational as well as maintenance costs.

 

 

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