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  • Published: 19 September 2016

Concentrating solar thermoelectric generators with a peak efficiency of 7.4%

  • Daniel Kraemer 1 ,
  • Qing Jie 2 ,
  • Kenneth McEnaney 1 ,
  • Feng Cao 2 ,
  • Weishu Liu 2 ,
  • Lee A. Weinstein   ORCID: orcid.org/0000-0001-8917-7547 1 ,
  • James Loomis 1 ,
  • Zhifeng Ren 2 &
  • Gang Chen 1  

Nature Energy volume  1 , Article number:  16153 ( 2016 ) Cite this article

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  • Thermoelectric devices and materials

Concentrating solar power normally employs mechanical heat engines and is thus only used in large-scale power plants; however, it is compatible with inexpensive thermal storage, enabling electricity dispatchability. Concentrating solar thermoelectric generators (STEGs) have the advantage of replacing the mechanical power block with a solid-state heat engine based on the Seebeck effect, simplifying the system. The highest reported efficiency of STEGs so far is 5.2%. Here, we report experimental measurements of STEGs with a peak efficiency of 9.6% at an optically concentrated normal solar irradiance of 211 kW m −2 , and a system efficiency of 7.4% after considering optical concentration losses. The performance improvement is achieved by the use of segmented thermoelectric legs, a high-temperature spectrally selective solar absorber enabling stable vacuum operation with absorber temperatures up to 600 ∘ C, and combining optical and thermal concentration. Our work suggests that concentrating STEGs have the potential to become a promising alternative solar energy technology.

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Acknowledgements

This material is partially based upon work supported as part of the Sunshot Initiative funded by the US Department of Energy, Office of Energy Efficiency & Renewable Energy under Award Number: DE-EE0005806 (for device engineering) and based upon work supported as part of the Solid State Solar-Thermal Energy Conversion Center (S 3 TEC), an Energy Frontier Research Center funded by the US Department of Energy, Office of Science, Office of Basic Energy Sciences under Award Number: DE-SC0001299/DE-FG02-09ER46577 (for materials).

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Department of Mechanical Engineering, Massachusetts Institute of Technology, Cambridge, Massachusetts 02139, USA

Daniel Kraemer, Kenneth McEnaney, Lee A. Weinstein, James Loomis & Gang Chen

Department of Physics and TcSUH, University of Houston, Houston, Texas 77204, USA

Qing Jie, Feng Cao, Weishu Liu & Zhifeng Ren

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Contributions

D.K. carried out modelling and simulation, CSTEG fabrication and experiments, and prepared the manuscript; Q.J. and W.L. fabricated the thermoelectric and contact materials; K.M. contributed to CSTEG fabrication and experiments and device modelling; F.C. fabricated spectrally selective solar absorbers; L.A.W. contributed to manuscript preparation and CSTEG fabrication and experiments; J.L. contributed to CSTEG fabrication and experiments; Z.R. directed research at UH; G.C. directed research at MIT and contributed to the manuscript preparation.

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Correspondence to Zhifeng Ren or Gang Chen .

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Kraemer, D., Jie, Q., McEnaney, K. et al. Concentrating solar thermoelectric generators with a peak efficiency of 7.4%. Nat Energy 1 , 16153 (2016). https://doi.org/10.1038/nenergy.2016.153

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Published : 19 September 2016

DOI : https://doi.org/10.1038/nenergy.2016.153

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Article Contents

Introduction, 1 hpvteg hybrid system description, 2 materials and methods, 3 experimental results and discussion, 4 economic analysis, 5 conclusions and future research recommendations, acknowledgements, author contributions, conflict of interest statement, data availability.

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Experimental study on hybridization of a PV–TEG system for electrical performance enhancement using heat exchangers, energy, exergy and economic levelized cost of energy (LCOE) analysis

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Mohammed A Qasim, Vladimir I Velkin, Sergey E Shcheklein, Experimental study on hybridization of a PV–TEG system for electrical performance enhancement using heat exchangers, energy, exergy and economic levelized cost of energy (LCOE) analysis, Clean Energy , Volume 7, Issue 4, August 2023, Pages 808–823, https://doi.org/10.1093/ce/zkad023

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The concept of employing thermoelectric generators (TEGs) to recover energy from waste heat has gained popularity, with applications that range from milliwatt to kilowatt levels of output power. In this study, a hybrid photovoltaic panel and thermoelectric generator (HPVTEG) system consisting of an integrated heat exchanger, a commercial polycrystalline silicon photovoltaic (PV) panel and a commercial bismuth telluride TEG was proposed. Here, TE components can be used to cool PV modules, increasing their output power via the Seebeck effect. The main finding is that the hybrid system has a reduced average temperature of 16.01°C. The average power of the stand-alone PV panel is 28.06 W, but that of the HPVTEG system is 32.76 W, which is an increase of 4.7 W. The conversion efficiency and power of the hybrid system increased by 16.7% and 16.4%, respectively, compared with a stand-alone PV panel. The HPVTEG system achieved an average exergy efficiency of 12.79% compared with 10.98% for a stand-alone PV panel. According to the calculation results, the levelized cost of energy (LCOE) of the stand-alone PV panel can range from 0.06741 to 0.10251 US$/kWh depending on how many days it is in operation, while the LCOE of the HPVTEG system can range from 0.06681 to 0.10160 US$/kWh.

Graphical Abstract

The need for energy is growing. Since natural resources are becoming scarcer, it is crucial to provide clean, reusable and ecologically friendly energy. The largest source of renewable energy, which can be directly transformed from light and heat to electricity, is solar energy [ 1–3 ]. Compared with a stand-alone photovoltaic (PV) system, combined PV and thermoelectric generator (TEG) systems have received considerable attention over the past 10 years and have been shown to be an excellent way to utilize waste solar heat [ 3–6 ]. Using a temperature differential between the back of the PV panel and the TEG cold junction, the Seebeck effect allows TEG modules to directly convert waste thermal energy into electricity. TEGs have several advantages since the heat supply is constant, they do not make noise, they are clean and they are compatible with PV systems. Furthermore, they can function for many years [ 7 , 8 ]. However, it is probable that the hybrid photovoltaic panel and thermoelectric generator (HPVTEG) efficiency is lower than that of PV systems alone [ 9 ]. Increased temperature differences will increase the efficiency of the TEG but reduce PV efficiency. Therefore, the connection between PV and TEG technology is complicated, which affects the performance of such systems [ 10 ].

Zhang et al. increased the open-circuit voltage and doubled energy harvesting. They developed a combination of polymer solar cells with thermoelectric (TE) modules [ 11 ]. Kil et al. concentrated on developing a PV/TE hybrid generator with a single junction. Their system used a GaAs-based solar cell and a conventional TE module. They found that the conversion efficiency of this hybrid system was 23.2% compared with 22.5% for a single PV cell. This improvement was ~3% at a solar intensity of 50 suns [ 12 ].

Rajaee et al. conducted studies on a system that included PV cells, TEGs (TEGs), nanofluids and phase-change materials. They found that the total electrical efficiency of the system could reach 15.8%. Moreover, they were able to increase the overall output by 42% [ 13 ]. Fini et al. conducted a 24-h analysis that involved experimental testing, mathematical modelling and finite-element simulation of a HPVTEG system using water-cooled heat exchangers that had been proposed to extract more power from the system. They found that the average maximum PV panel temperature in both the experimental measurements and the simulations of the hybrid system was 44.2°C at maximum irradiation, while it was 57.1°C for a reference PV panel. Furthermore, they found that the efficiency of a pure PV panel was 13.82% while that of its hybrid systems was 15.6% [ 14 ].

Mahmoudinezhad et al. tested the performance of PV, TEG and HPVTEG systems using a spectrum beam splitter. According to the results of their analysis, the system that used only TEGs generated more power than the TEG in the hybrid system because it made better use of the whole spectrum of energy available to it. While the efficiency of the TEG component decreased, the total efficiency of the hybrid system improved due to the increased PV efficiency. The hybrid system produced more power than either the PV or TEG systems individually [ 15 ].

Lorenzi et al. designed a Bi 2 Te 3 TEG device for hybridization with three distinct panels. These were amorphous silicon (a-Si), gallium indium phosphide (GaInP) and perovskite PV panels. At an intensity of 5 suns and a panel temperature of 340 K, the perovskite panel had the greatest efficiency improvement among three HPVTEG systems. Then, they experimentally constructed a perovskite HPVTEG model. Their tests revealed a change in efficiency from 16.8% to 19.5%—a 16.07% improvement [ 5 ].

Babu et al. also used the MATLAB ® /Simulink ® environment to do a theoretical study of a non-concentrating hybrid HPVTEG system. This hybrid system was 6% more efficient overall and could produce 5% more energy [ 16 ]. Shatar et al. considered the load requirements of an indoor farm to design an unconcentrated PV–TEG hybrid system. The performance of the hybrid system was evaluated during 3 months of testing in Malaysia. The planned system was proven to be able to accommodate an additional load while also providing enough power to service its intended load [ 17 ].

Van Sark did direct coupling to combine TE modules with solar cells to create a hybrid HPVTEG system that achieved improved electrical performance [ 18 ]. This technology was offered as an efficient thermal management strategy for PV cells. Two case studies were provided from Utrecht, The Netherlands and Malaga, Spain. The results also indicated that the energy of Malaga and Utrecht could increase by ~14.7% and ~11%, respectively, using the annual irradiance and temperature profiles of these cities. However, this study overlooked radiation losses and the idealized model overstated the results for real HPVTEG systems by ~10% [ 18 ].

Ko et al. used MATLAB ® software to quantitatively examine the transient behaviour of a HPVTEG system incorporated into a building in combination with phase-change materials (PCMs). They investigated the impact of the PCM layer thickness and melting point on the HPVTEG efficiency. According to their findings, the hybrid system was 1.09% more efficient than a PV system alone, with 0.18% coming from TEGs and 0.91% from PVs. Furthermore, the proposed system produced 0.91% more energy in spring, 1.32% more in summer, 2.25% more in autumn and 3.16% more in winter. It was suggested that the hybrid system might possibly produce 4.47% more power than a single PV system when TEGs with higher figure of merit were employed [ 19 ].

Beeri et al. presented experimental and theoretical data for a combined HPVTEG system to convert concentrated sunlight, with a factor of X of ≤300, into electricity. These results demonstrate that when the X-value and system temperature were increased, the efficiency of the PV cell decreased and that of the TEG increased. As a result, the direct electrical contribution of the TEG began to predominate in the overall system, reaching a 20% power contribution at an X-value of 290. Efficiency changed from 28.95% to 30.53% with an improvement of 5.45% at a concentration factor of 205. Using more sophisticated PV cells and TE materials, it was demonstrated that the hybrid system may exceed 50% overall efficiency [ 20 ].

Khan et al. demonstrated an experimental PV–TEG system. A 10-W polycrystalline silicon panel with 10 bismuth telluride TEG modules was mounted on the back of the panel to recover and convert waste heat into usable electrical energy, while simultaneously cooling the PV cells. The results showed that this hybrid system achieved increased output power and conversion efficiency values for PV modules. In the hybrid system, the operating temperature of the PV module decreased by 5.5%, from 55°C to 52°C. Compared with a straightforward PV system, the total output power of the hybrid system increased from 8.78 to 10.84 W—a 19% increase. Furthermore, the efficiency of the HPVTEG system increased from 11.6% to 14%—a total improvement of 17% [ 21 ].

Li et al. showed inconsistency of TE load resistance for PV–TE modules from a theoretical perspective. Two types of PV cells were employed to build and test a model PV–TE. Under various working conditions for a TE module, a TE in the PV–TE and a PV–TE, the maximum load resistance of each TE was examined. The efficiency of crystalline silicon alone was 9.5% and increased to 11.07% in a hybrid system with a TE load resistance of 0.75 and a figure of merit of 0.0085/K. The efficiency of GaAs alone was 21.91% and this increased to 22.94% in the hybrid mode when the TE load resistance was 1.60 and the figure of merit was 0.0022/K [ 22 ].

Zhang et al. used 3D numerical modelling to calculate the potential and characteristics of an integrated system consisting of new perovskite solar cells and TE modules. They found that the temperature coefficient of the perovskite solar cell was <2%. Due to such a reduced temperature coefficient, the efficiency of the perovskite solar cell–TEG hybrid system was 18.6%, while that of a pure perovskite solar cell was 17.8%, making it a good alternative in a HPVTEG system. The heat can be changed, and thus the required bulk TEG material may be reduced, leading to significant cost savings for a hybrid system [ 23 ].

Cui et al. experimentally utilized a PCM to develop a unique PV–PCM–TE hybrid system to maintain system function at an optimal temperature. The temperature, efficiency and output power of the hybrid system were compared with those of a stand-alone PV system under identical conditions. The effects of the optical concentration ratio and cooling approach on the conversion efficiency of the hybrid system were experimentally explored. According to the results, the hybrid PV–PCM–TE system had an efficiency of 13.45%, compared with that of a stand-alone system of 13.43%. The study indicated that such a hybrid system has good potential for full-spectrum conversion of solar energy [ 24 ].

Generally, previous studies do not consider some issues. Most HPVTEG systems link many TE modules in a series and parallel array to achieve the necessary power level. The uniform temperature distribution of the TE modules, the influence of the pressure distribution on the assembly, the thermal contact between the modules and the heat exchangers, and the thermal bridge between the heat exchangers and the PV panel were not given much attention. Additionally, the issues of concentrated and non-concentrated solar irradiation techniques were given little consideration in HPVTEG systems. For non-concentrated HPVTEG systems, the electrical performance of PVs and the gradient temperature for TEGs are low, and most of the electricity is produced by the PVs. However, for concentrated HPVTEG systems, the operating temperature of the PV system increases, sometimes to levels of >100°C, significantly reducing its performance. This led to high temperature gradients for TEGs and increased electricity production.

Therefore, the creation of a hybrid system that balances the performance of solar panels and TEGs, with appropriate electrical connections and assembly of TEG modules to obtain the appropriate voltage, is extremely important, where the modules are attached to the back of generic PV panels. In this work, a TEG configuration test method was used to measure and analyse data obtained from TEGs, one of which was highly efficient in the proposed system. In addition, a HPVTEG system was fabricated using an experimental design for the Iraqi climate using analysis of energy, exergy and economic levelized cost of energy (LCOE). The overall objective of the current research is to quantify the performance of this system and its associated parameters with the goal of enhancing the conversion efficiency and heat recovery of a PV panel in a hybridized system (HPVTEG) for comparison with a stand-alone PV panel.

A hybrid HPVTEG system paired with water-cooled heat exchangers was fabricated to study the heat recovery and cooling of a PV panel and capture of a greater portion of the solar spectrum. This is one option to improve the efficiency of PV technologies [ 25–28 ]. Fig. 1 shows the configuration of the hybrid system, which consists of two solar panels mounted on an iron structure that is tilted at a 33° angle towards the south.

The proposed system. (a) Experimental set-up system with measurement devices and (b) schematic diagram of the experimental system.

The proposed system. (a) Experimental set-up system with measurement devices and (b) schematic diagram of the experimental system.

1.1 Main and subsystem components

1.1.1 pv panel.

PVs play a crucial part in determining the final output of the system. Two polycrystalline PV panels, manufactured by Fortuner, were chosen for this experiment; they have a nominal maximum power of 50 W, a power coefficient of 0.004/K and an efficiency of 14.51% under standard test conditions (STC): sea level air mass (AM) = 1.5, 1000 W/m 2 cell temperature, 25°C. Table 1 highlights the properties of the PV panel [ 29 ].

PV panel properties

1.1.2 TEG module

A semiconductor-based device, known as a TEG, serves as a tiny generator using the Seebeck effect when a temperature differential is applied to its surfaces. TEG modules made from bismuth telluride (Bi 2 Te 3 ) are employed to produce the required power. These modules were created specifically for power generation. Table 2 lists the characteristics of the TEG module [ 7 , 15 ].

Thermoelectric module properties

1.1.3 Poly(methyl methacrylate)

Generally, heat exchangers or the TE modules themselves are taken into account when optimizing TEGs [ 30 , 31 ]. However, since poor contact or a thermal bridge can undermine the performance of a perfect generator, consideration of the entire assembly of the TEG is crucial. This is to control the impact of the pressure distribution on the assembly, as well as the thermal contact resistance between the modules, the heat exchangers and the thermal bridge between the exchangers. Poly(methyl methacrylate) (PMMA), an acrylic, was considered with dimensions of 142.5 × 455 mm 2 . It has specific qualities that make it a good material for use in a variety of applications. This thermoplastic is ideal for joining TEG pieces to aluminium sheets to sandwich a PV module, due to its excellent thermal insulation properties and high resistance to temperature changes [ 32 ].

1.1.4 Heat exchanger cooling

An aluminium water block was utilized to dissipate heat from the cold side of the TEG and rear PV panel. The dimensions of each piece were 40 × 240 × 10 mm 3 . The parameters of the heat exchanger and some characteristics of water are shown in Table 3 , where these values were extracted by numerical analysis during our earlier work [ 33 ].

Heat exchanger parameters and water properties

1.1.5 Mathematical expressions and governing equations

In this section, the HPVTEG system governing equations, as well as its energy and exergy analyses, are considered.

1.2 Computation of energy

1.2.1 solar pv subsystem.

The reduction in operating temperature (caused by the TE device) is the main source of the performance improvement for solar cells integrated into a HPVTEG configuration. Therefore, it is necessary to describe the performance parameters of the cell with respect to temperature to determine the source of improvement [ 34 ]. Using Equation (1), it is possible to determine the PV cell efficiency η m p p ( G , T p v ) for an operating temperature T p v [ 35 ]:

where T r e f represents the reference air temperature and G is the incident solar irradiance. The temperature efficiency coefficient, often given by the cell manufacturer, is denoted by β ⁠ , while η m p p ( G , T r e f ) represents the PV cell efficiency at STC.

After defining the PV conversion efficiency η m p p ( G , T p v ) ⁠ , Equation (2) may be used to calculate the PV cell power output at a previously determined temperature T p v   [ 36 ]:

where A is the solar-facing frontal area of the PV cell.

1.2.2 TE subsystem

Each TEG thermocouple has p- and n-junctions (legs). Thermal transmission losses, as well as electrical and thermal contact resistances, are neglected. At steady state, the power is absorbed at the hot side of the TEG module and the power is discharged at the cold junction [ 37 ], as follows:

In Equations (3) and (4), the first terms on the left-hand side indicate Peltier heat in power transmission, whereas the second and third terms imply Joule and Fourier heat in power transmission. Internal resistance ( R ) and thermal conductance ( K ) are expressed as [ 38 ]:

where α is the Seebeck coefficient; ρ p and ρ n are the densities of the legs; l T E G l is the TEG leg length; and A p and A n are the cross-sectional areas of the TEG legs, which are equal.

Using the difference P h − P c ⁠ , the output power of the system may alternatively be represented as current and load resistance, R L ⁠ :

Additionally, the current and Seebeck electromotive force (e.m.f.) can be calculated as:

Combining Equations (3), (4), (8) and (10), the efficiency of the TEG module can be expressed as Equation (11) [ 39 ]:

where β = R l R ⁠ , Z p , n = α 2       ρ k and η c = T h − T c T h .       The maximum efficiency occurs at β = R l R = ( 1 + Z T ) 0.5 ⁠ , where T h and       T c       are averaged to yield T ⁠ :

1.2.3 HPVTEG system

A hybrid system was developed that combined PV and TEG modules with four wires in parallel for an isolated load, where the energy-harvesting process was executed separately. This system is illustrated in Fig. 2 as its equivalent electrical circuit.

Circuit diagram for the HPVTEG system.

Circuit diagram for the HPVTEG system.

The solar energy, Q , illuminates the PV cell, which produces electricity, p p v ⁠ . Heat is produced that is not converted to electricity by the PV cell, which is then transferred to the hot side of the TEGs, transforming it into extra electrical power   p t e g that is removed from the system on the cold side of the TEGs. Equations (13) and (14) provide the total system electrical power output p t o t and efficiency η t o t [ 40 ]:

where Q is the incident solar irradiance input energy, which is equal to G ⋅ A ⁠ , where G and A are the Sun intensity and solar module area.

1.2.4 Exergy modelling

This section presents a detailed exergy analysis of the HPVTEG system under investigation. Exergy analysis is a helpful technique for contrasting the actual and desired performance of the system. By lowering the exergy destruction parameters, the performance of the device is enhanced. Calculating exergy efficiency is as follows [ 41 ]:

where E x t o t is the total quantity of exergy obtained and E x i n is the input exergy of the system; they can be obtained by using [ 41 ]:

where G is the solar radiation, A PV is the panel aperture area, T amb is the surrounding air temperature and T s is the temperature of the energy source (the Sun). The exergy acquired from the water, PV and TEGs is denoted as E x t h ⁠ , Ex PV and Ex TEG ⁠ , and they can be obtained by using [ 42 ]:

In these equations, m ˙ w represents the mass flow rate of a coolant fluid and c P w is its heat capacity. T o u t w and T i n w are the water inlet and outlet temperatures. The PV reference efficiency is denoted by   η   ref ⁠ , while the PV efficiency temperature coefficient is β r e f and the PV temperature is T p v ⁠ . P T E G and P c represent the output power and the power absorbed by the TEGs, respectively. P c           can be obtained by using [ 42 ]:

where n is the number of thermocouples of the TEG, α is the Seebeck coefficient, and I , R and K are the electric current, electrical resistance and thermal conductivity of the TEGs, respectively. The parameters of the PV panel and the TEG found in [ 43–47 ] and those of the heat exchanger are given in Section 1.1.4 [Heat exchanger cooling].

2.1 Experimental set-up

This section presents the techniques and materials required to fabricate the experimental set-up and the techniques to record the experimental data.

2.1.1 TE module

It is necessary to take advantage of the heat produced during PV cell operation and ensure that the hybrid system performance is better than that of the non-hybrid systems. Two electrical configurations were considered for TEGs.

2.1.2 Experiment 1: Configuration-1-SP

Series and parallel array configurations (Configuration-1-SP) with 20 TEGs are suggested. This configuration used two groups of 10 TEG modules connected in series. Then, the two groups were connected in parallel. Fig. 3 shows an equivalent circuit for this configuration.

Equivalent circuit of the Configuration-1-SP thermoelectric generator.

Equivalent circuit of the Configuration-1-SP thermoelectric generator.

2.1.3 Experiment 2: Configuration-2-SP

In Configuration-2-SP, groups with two TEG modules are connected in series. Then, 10 groups were connected in parallel. Fig. 4 shows the equivalent circuit of this configuration.

Equivalent circuit of the Configuration-2-SP thermoelectric generator.

Equivalent circuit of the Configuration-2-SP thermoelectric generator.

Then Configuration-1-SP was considered in this work. This configuration is used to make the internal resistance, R i n ⁠ , approximately equal to the external load, to improve electrical performance, since the maximum power can be achieved when ( R in is R Load).

2.1.4 Assembly of the HPVTEG system

As shown in Fig. 1 , the assembly used TEG modules attached to a sheet of aluminium 6061, affixed to the rear of the PV panel with thermal paste. Four heat exchangers were attached underneath each group of five TEG modules. These heat sinks were attached to the TEG modules using thermal paste to improve heat transfer. Finally, thermoplastic PMMA was used for joining the TEG to the PV module, fixing it to the frame. Silicon water tubes were used to connect the heat sinks to a tap water source. Tap water was selected as a cooling fluid because it is readily available in homes and there is no need for a circulation pump. It is quite suitable for heat transfer because of its low cost and high heat capacity. The water flow rate was an approximately constant (2.56 L/min) at ~23°C throughout the experiment. The water circulates through the heat exchanger and is returned to the homes.

The temperatures of the PV cell and the TEG hot side that provides the heat input were considered to be equal throughout the experiment. The temperatures of the hot and cold sides of the TEGs as well as the inlet and outlet water temperatures of their corresponding heat sinks were measured using K-type thermocouples. The operating temperature of the solar panel was measured using a separate thermocouple attached to the rear of the PV panel. Measured values from multiple thermocouples were transmitted directly to a microcontroller and saved on a Secure Digital (SD) memory card.

The approach used in this study is unique and simple. In most studies, the TEGs are individually fixed to the rear side of the panel. In the current study, we attached the TEGs as groups with an appropriate electrical configuration for an individual panel.

The cooling mechanism employed in this study also allows the back of the PV panel to be cooled by the TEG panels, i.e. the cooling block water, since the TEG panels do not cover the entire back surface of the solar panel. The complete experimental set-up is provided in Fig. 5 .

Overview of the experimental set-up of the HPVTEG system. (a) Final experimental set-up with Configuration-1-SP and (b) schematic of the experimental set-up.

Overview of the experimental set-up of the HPVTEG system. (a) Final experimental set-up with Configuration-1-SP and (b) schematic of the experimental set-up.

The experimental results of the TEG and hybrid HPVTEG systems are discussed in this section, as well as the results of the hybrid system compared with a stand-alone PV panel operated under the same conditions. The experiments were carried out in July, during the summer, in Baghdad, Iraq. The geographical coordinates were latitude 33.313 o N and longitude 44.331 o E. Testing was carried out from 9:00 h to 16:30 h. The measurements were made at ~15-minute intervals.

3.1 Environmental impact and analysis

The radiation profile, relative humidity, wind speed and air temperature during the testing period are shown in Figs 6 and 7 , drawn using Origin software [ 48 ] to develop curves for radiation and temperature. The findings show that solar irradiance increased steadily over time. The average solar irradiance of 783.18 W/m 2 peaked at noon with an instantaneous value of 963.07 W/m 2 and began to decline thereafter. The averages of outside temperature, relative humidity and wind speed were 42.61°C, 11.70 and 1.88 m/s, respectively. The wind velocity varied from ~1.0 to 2.2 m/s.

Solar radiation and air temperature during the experimental runtime.

Solar radiation and air temperature during the experimental runtime.

Relative humidity and wind speed during the experiments.

Relative humidity and wind speed during the experiments.

3.2 Temperature effects

3.2.1 analysis of the teg temperatures profile.

Since the air temperature peaked at 13:00 h, the hot- and cold-side temperatures, Δ T , similarly peaked at this time and then fell, as illustrated in Fig. 8 . The TEG hot side ( ⁠ T h ⁠ ) showed high and low temperatures of 51.49°C and 35.08°C, respectively, with an average temperature of 44.97°C. When the experiment first began, T c was low on the cold side. After noon, it gradually decreased, as heat accumulated in the water and reached an equilibrium. Low and high cold-side temperatures were 24.88°C and 27.55°C, respectively, with an average temperature of 26.71°C. The temperature difference ( ⁠ Δ T ⁠ ) between the hot and cold sides of the ranged between 10.21°C and 24.06°C, respectively, with an average temperature difference of 18.25°C. These temperatures were measured using thermocouples and a microcontroller to provide more precise results.

Hot-side and cold-side temperatures of the TEGs, with temperature differentials at various times.

Hot-side and cold-side temperatures of the TEGs, with temperature differentials at various times.

3.2.2 HPVTEG system temperature profiles

The PV panel temperature is a crucial component since it determines the performance of the system. Fig. 9 displays a temperature–time curve for HPVTEG and stand-alone systems. Each PV panel had five K-type thermocouples installed in various places to provide measurements every 15 minutes.

PV modified and stand-alone PV panel temperatures as a function of time.

PV modified and stand-alone PV panel temperatures as a function of time.

According to Fig. 9 , the temperatures of the HPVTEG system and stand-alone PV panel increased throughout the day until they reached a maximum at 13:00 h. The maximum, minimum and average temperatures of the HPVTEG system during the testing were 51.49°C, 35.08°C and 44.97°C, and 67.76°C, 52.86°C and 60.98°C for the stand-alone panel, respectively. This represents a 16.01°C cooler operating temperature for the HPVTEG system compared with a stand-alone module.

This reduction is significant, especially considering that this process uses little circulation water to remove heat from the cold side of the TEGs and no electricity is used to cool the PV module. As a result, this system can be used in regions with readily accessible tap water or as geothermal technology in areas without water.

3.2.3 Heat exchangers

The input and output water temperature profiles of the four heat exchangers are shown in Fig. 10 . The input water temperatures were approximately constant, at ~23°C, during the experiment. The output water temperature was greater than its input temperature, as shown in this figure, as a result of increased TEG cold-side temperatures, which averaged 25.92°C with a maximum value of 26.79°C. The output water temperature peaked at 13:15 h, at the same time as the cold-side TEG temperature, but there was a 15-minute lag in the temperature of the PV panel, since its cooling water was slower to lose heat.

Input and output temperatures of a heat exchanger as a function of time.

Input and output temperatures of a heat exchanger as a function of time.

3.3 Electrical energy assessment

3.3.1 teg configuration analysis.

Fig. 11 shows the results of power and efficiency from the two TEG electrical configurations. Since the temperature was the same for each set-up during the experiment, the power extracted and efficiency varied, with Configuration-1-SP achieving the highest performance. This came from the type of TEG electrical connections. According to the findings, the average output power and efficiency of Configuration-1-SP were 1.24 W and 0.51 ⁠ , while they were 0.20 W and 0.08% for Configuration-2-SP, respectively.

Electrical configurations of TEGs. (a) Output power versus time; (b) efficiency versus time.

Electrical configurations of TEGs. (a) Output power versus time; (b) efficiency versus time.

3.3.2 HPVTEG system

Figs 12 and 13 display the output power and efficiency values for the HPVTEG system and stand-alone panel. Statistics show that at 12:00 h, the maximum power output of the HPVTEG system was 39.97 W, while the peak power of the stand-alone panel was 33.99 W. However, since the stand-alone panel operated at a relatively high temperature, it suffered a power reduction. Throughout the tests, the HPVTEG system and the stand-alone panel average power values were 32.76 and 28.06 W, respectively. The HPVTEG system shows an average improvement of 16.7 ⁠ .

Output power of the HPVTEG and stand-alone PV systems.

Output power of the HPVTEG and stand-alone PV systems.

Electrical efficiency versus time for the HPVTEG and stand-alone PV systems.

Electrical efficiency versus time for the HPVTEG and stand-alone PV systems.

Until midday, the intensity of the solar radiation helps to raise the power extracted from both the HPVTEG system and the stand-alone panel. However, the electrical efficiency of the HPVTEG system and the stand-alone panel began to decrease as a result of the increase in operation temperature, and then after noon the electrical efficiency returned to increase as a result of the decrease in the temperature of the HPVTEG system and the stand-alone panel as shown in Fig. 13 . The HPVTEG system had an average efficiency of 13.86% compared with the PV stand-alone panel, at 11.90%. This is because of the high temperatures that were recorded throughout the period of the experiment for the stand-alone PV panel. The electrical efficiency of the HPVTEG system was improved by ~ 16.4

Since the hybrid system used TEGs and heat exchangers, this efficiency improvement is very significant. This resulted in a lower panel operating temperature that allowed more power extraction from the TEGs.

3.3.3 Exergy efficiency assessment analysis

Fig. 14 shows the exergy efficiency results of the HPVTEG system and stand-alone PV panel. The power output of a power plant has a negative impact on its energy efficiency. The profiles for the energy efficiency for the two systems can thus be observed from the data, since they are similar to those for the electrical efficiency.

Exergy efficiency of stand-alone and HPVTEG systems versus time.

Exergy efficiency of stand-alone and HPVTEG systems versus time.

The exergy efficiency decreased from the beginning of the experiment until about 13:00 h, when it began to increase due to increased PV module temperatures. The exergy of the HPVTEG system was consistently greater throughout the testing, indicating that the suggested hybrid system can be used to control the temperature of the PV module.

As a result, the average exergy efficiencies for the HPVTEG system and the stand-alone PV panel, respectively, were 12.79% and 10.98%. It is clear from the data that the modified PV panel had a higher exergy efficiency.

3.3.4 Measurement error analysis

Measurement accuracy, test system design specifics and human error affect the accuracy of experimental findings. Table 4 , derived from measuring equipment, lists experimental errors that could exist in the parameters utilized.

Measurement uncertainties of various devices

Using previously published error analysis methodology [ 49–52 ], the total percentage of uncertainty u ( z ) can be calculated using Equation (22):

where Z ⁠ ,       Δ   y 1 ,   Δ   y 2 , . . .   Δ   y n are dependent variables of various inputs, in which potential errors may exist. The total percentage of uncertainty in the proposed system used in these experiments is 3.87%, which is considered allowable in the context of a study such as this.

3.3.5 Examining the system in relation to other researches

Table 5 compares our findings with the research discussed above and other studies. Generally, the results are superior or equivalent to the systems described in prior investigations.

Comparison of the current system to previous studies

An LCOE strategy was employed to analyse energy production costs for the proposed system. This strategy is often used to evaluate the economic feasibility of renewable-energy facilities. It indicates the costs in a way that compares various power producing methods on a normalized basis [ 53 , 54 ]. The LCOE is described as the lowest cost at which the energy produced must be sold to financially break even during the life of the project [ 55 , 56 ]. Additionally, it assesses the average overall cost of building and operating a power plant over the course of its lifetime divided by the total amount of energy produced during that period. The mathematical formulation of the LCOE is [ 57 ]:

where the investing cost is C inv , n is the plant lifetime, CRF is the capital recovery factor, C O&M represents the yearly operation and maintenance expense, CELF is the constant-escalation laterization factor, i eff represents the effective discount rate and r n is the nominal escalation rate.

The main production expenditures in the proposed HPVTEG system are heat exchangers and TEGs, requiring two sets of TEGs at a price of US$15.2, and four heat exchangers at a price of US$2, based on year 2022 data. In general, the HPVTEG system and associated equipment cost US$71.2 with a solar panel price of US$54.

This study considered two possibilities for the energy produced by the power plant:

(i) The first case entails circumstances in which the power plant operates all year with no bad weather. Every day of the year is used to produce electricity in this case.

(ii) The second case also considers a situation with favourable weather for only a portion of the year, such as that in Iraq. This considers Iraq’s 8-month summer season, or 240 days, as productive in this case.

Assumptions were made that the panel would be exposed to solar radiation for 10 h a day for 365 and 240 days, respectively. The energy output from the HPVTEG power plant and the stand-alone panel in the first and second cases was (120.09 kWh, 78.96 kWh) and (102.42 kWh and 67.34 kWh), respectively. Then we used the information in Table 6 to determine the LCOE of both systems.

Calculation of LCOE parameters

According to the calculations, the HPVTEG system LCOE in the first case, with 365 days of production, was 0.06681 US$/kWh as opposed to 0.06741 US$/kWh for the stand-alone PV panel. Furthermore, the HPVTEG hybrid system showed an LCOE of 0.10160 US$/kWh for the second case with 240 days of production compared with 0.10251 US$/kWh for the stand-alone PV panel.

These data clearly show that the HPVTEG hybrid system outperformed the stand-alone PV panel in terms of cost under both scenarios, despite the additional costs associated with integrating the TEG with the PV panel. This implies that adding the suggested TEG mechanism to a PV module will increase its cost-effectiveness in addition to improving its electrical and exergy efficiency.

TEGs and heat exchangers were used to improve the functionality and lower the operating temperature of a PV panel while using the whole solar spectrum in an HPVTEG system. Current research enables the following conclusions to be drawn:

(i) Efficiency and output power are significantly improved using the HPVTEG system. This results from the use of water by the HPVTEG system as a cooling medium, rather than unstable and variable cooling sources. This system is independent, economical and has no complicated mechanisms.

(ii) The use of the PMMA board serves three functions: cohesion, good pressure distribution and insulation. This led to an improvement in the power of the TEG modules.

(iii) There was an average temperature difference ( ⁠ Δ T ⁠ ) of 18.25   °C between the hot and cold sides of the TEGs.

(iv) During experimentation, the average HPVTEG system temperature was 44.97   °C compared with 60.98   °C for the stand-alone PV panel. Therefore, the use of the TEG module with cooling resulted in an average temperature that was 16.01°C lower for the HPVTEG system.

(v) During the experiments, the average water temperature at the exit of the heat exchanger was 25.92°C.

(vi) Among the TEG configurations, the average power and efficiency for Configuration-1-SP were 1.24 W and 0.51 ⁠ , whereas those for Configuration-2-SP were 0.20 W and 0.08%, respectively.

(vii) The average power output for the HPVTEG system was 32.76 W, whereas that of the stand-alone PV panel was 28.06 W. The increase in electricity generation is 4.7 W in total—an average improvement of 16.7 ⁠ .

(viii) The average efficiency of the HPVTEG system was 13.86%, while the efficiency for the stand-alone PV panel was 11.90%. The increase in electricity generation is 1.96% in total—an improvement of ~16.4%.

(ix) There is an average difference of 1.81% in the exergy efficiency between the stand-alone PV panel and the HPVTEG system.

(x) Financially, in the first scenario (365 days of production), the HPVTEG system had an LCOE equivalent to 0.06681 US$/kWh compared with 0.06741 US$/kWh for the stand-alone PV panel. Furthermore, the HPVTEG system showed an LCOE of 0.10160 US$/kWh for the second case (240 days of production) compared with 0.10251 US$/kWh for the stand-alone PV panel.

In practice, the HPVTEG mechanism has been shown to be technologically and economically better. The proposed hybrid mechanism shows the lowest LCOE due to its high efficiency, even if its modifications come at an additional cost.

According to the findings of this study, it is possible to use the suggested cooling mechanism and the TEG module in hot climates, such as Iraq, to improve the performance of solar PV panels and produce more power.

More TEGs might be used to cover the back of the solar panel, but future research should also consider the financial implications of this action. Future research may look towards using a nanofluid rather than water to dissipate more heat from the PV panel.

The research funding from the Ministry of Science and Higher Education of the Russian Federation (Ural Federal University Program of Development within the Priority-2030 Program) is gratefully acknowledged (grant number FEUZ-2022-0031). This research project received no external funding.

Conceptualization, M.A.Q. and V.I.V.; methodology, M.A.Q.; software, M.A.Q.; validation, M.A.Q., S.E.S. and V.I.V.; formal analysis, M.A.Q. and V.I.V.; investigation, M.A.Q.; resources, S.E.S. and M.A.Q.; data curation, M.A.Q. and S.E.S.; writing—original draft preparation, M.A.Q.; writing—review and editing, M.A.Q.; visualization, M.A.Q., supervision, V.I.V.; project administration, M.A.Q.; funding acquisition, M.A.Q. All authors have read and agreed to the published version of the manuscript.

The authors declare that they have no conflicts of interest that could have affected the design and conduct of the study, its conclusion or technical implications.

All important data are included in the manuscript.

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Design of a Concentration Solar Thermoelectric Generator

  • Published: 09 June 2010
  • Volume 39 , pages 1522–1530, ( 2010 )

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thesis solar thermoelectric generator

  • Peng Li 1 ,
  • Lanlan Cai 1 ,
  • Pengcheng Zhai 2 ,
  • Xinfeng Tang 1 ,
  • Qingjie Zhang 1 &
  • M. Niino 3  

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Thermoelectric technology can be another direct way to convert solar radiation into electricity, using the Seebeck effect. Herein, a prototype concentration solar thermoelectric generator (CTG) and a discrete numerical model for the evaluation of the whole system are presented. The model takes into account the temperature dependence of the thermoelectric material properties by dividing the thermoelectric leg into finite elements and is proved to be more accurate for calculation of the conversion efficiency of the thermoelectric modules when large temperature gradients occur in the CTG system. Based on the best available properties of various bulk thermoelectric materials reported in the literature, the best possible performance of the CTG system is predicted, and the CTG system design, including the selection of the concentration ratio and the cooling method for different thermoelectric materials, are discussed in detail.

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Abbreviations.

Solar irradiance (W/m 2 )

Concentration ratio

Absorptivity of the collector coating

Emissivity of the collector coating

Stefan–Boltzmann constant ( σ SB  = 5.67 × 10 −8  W/m 2  K 4 ).

Incident sunlight energy on a Fresnel lens (W)

Heat absorbed by the collector (W)

Energy reradiated from the collector surface (W)

The sum of heat losses (W)

Heat absorbed by the hot junction of the thermoelectric module (W)

Heat rejected by the cold junction of the thermoelectric module (W)

Power output of a thermoelectric module (W)

Optical efficiency of the Fresnel lens

Energy loss ratio

Conversion efficiency of the thermoelectric module

Efficiency of the CTG

Area of the lens, collector, and heat sink (m 2 )

Cross-sectional area of either the p - or n -type leg (m 2 )

Number of thermocouple pairs in a thermoelectric module

Length of the p - or n -type leg (m)

Length of the i th subsection (m)

Numbers of p - and n -type legs

Temperature of the collector surface and of the environment (K)

The hot-junction and cold-junction temperature of the thermoelectric module (K)

Interface temperature between the i th and ( i  + 1)th subsections (K)

Conductivity of the thermoelectric materials at temperature T i (S/m)

Thermal conductivity of the thermoelectric materials at temperature T i (W/K/m)

Seebeck coefficient of the thermoelectric materials at temperature T i (V/K).

Seebeck coefficient of the i th subsection (V/K)

Thermal conductivity of the i th subsection (W/K)

Resistance of the i th subsection (Ω)

Total internal resistance of the thermoelectric module (Ω)

Contact electrical resistance of the hot junction and cold junction (Ω)

Electrical current through the circuit under matched-load conditions (A)

Heat transfer coefficient of the heat sink (W/K/m 2 )

p - and n -type thermoelectric materials

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Acknowledgements

The authors acknowledge financial support from the Hi-TECH Research and Development Program of China (Grant No. AA05Z444), the National Basic Research Program of China (Grant No. 2007CB6 07506), and the National Natural Science Foundation of China (Grant No. 50930004).

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State Key Laboratory of Advanced Technology for Materials Synthesis and Processing, Wuhan University of Technology, Wuhan, 430070, China

Peng Li, Lanlan Cai, Xinfeng Tang & Qingjie Zhang

Department of Engineering Structure and Mechanics, Wuhan University of Technology, Wuhan, 430070, China

Pengcheng Zhai

Japan Aerospace Exploration Agency, Kakuda, Miyagi, 981-1525, Japan

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Li, P., Cai, L., Zhai, P. et al. Design of a Concentration Solar Thermoelectric Generator. J. Electron. Mater. 39 , 1522–1530 (2010). https://doi.org/10.1007/s11664-010-1279-0

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Received : 10 July 2009

Accepted : 07 May 2010

Published : 09 June 2010

Issue Date : September 2010

DOI : https://doi.org/10.1007/s11664-010-1279-0

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Energy & Environmental Science

Concentrated solar thermoelectric generators †.

* Corresponding authors

a Materials Science, Colorado School of Mines, Golden, CO 80401, USA

b Materials Science, California Institute of Technology, Pasadena, CA 91125, USA

c Department of Physics, Colorado School of Mines, Golden, CO 80401, USA E-mail: [email protected]

Solar thermoelectric generators (STEGs) are solid state heat engines that generate electricity from concentrated sunlight. In this paper, we develop a novel detailed balance model for STEGs and apply this model to both state-of-the-art and idealized materials. This model uses thermoelectric compatibility theory to provide analytic solutions to device efficiency in idealized materials with temperature-dependent properties. The results of this modeling allow us to predict maximum theoretical STEG efficiencies and suggest general design rules for STEGs. With today's materials, a STEG with an incident flux of 100 kW m −2 and a hot side temperature of 1000 °C could achieve 15.9% generator efficiency, making STEGs competitive with concentrated solar power plants. Future developments will depend on materials that can provide higher operating temperatures or higher material efficiency. For example, a STEG with zT = 2 at 1500 °C would have an efficiency of 30.6%.

Graphical abstract: Concentrated solar thermoelectric generators

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Concentrated solar thermoelectric generators

L. L. Baranowski, G. J. Snyder and E. S. Toberer, Energy Environ. Sci. , 2012,  5 , 9055 DOI: 10.1039/C2EE22248E

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Proposal of a new low-temperature thermodynamic cycle: 3E analysis and optimization of a solar pond integrated with fuel cell and thermoelectric generator

  • Musharavati, Farayi
  • Khanmohammadi, Shoaib
  • Gogoi, T. K.

The present research deals with a novel hybrid system that comprises of a salinity gradient solar pond (SGSP) integrated with a proton exchange membrane fuel cell (PEMFC) and a thermoelectric generator (TEG). The key novelty of this research is the use of PEMFC waste heat to increase the performance of the low-temperature heat source (solar pond). Also, a thermoelectric generator is employed in the proposed setup for complete waste energy recovery. In this paper, the proposed system's energy, exergy, and economic (3E) performance are investigated, as well as compared with two additional systems that were modelled by excluding TEG and PEMFC to showcase the benefits of the sub-systems in the final configuration. A parametric study is also conducted to investigate the effect of significant parameters on the overall system performance. The simulation results indicated that the integrated system's net output power is 2288.8 kW at a base case operating condition, with energy and exergy efficiency of 11.26% and 13.17%, respectively, and a system cost rate of 394 $/h. In comparison to other components in the integrated system, SGSP alone accounts for 75% of total exergy degradation and has the highest investment cost rate of 66.70 $/h. Further, to achieve the best system performance, a multi-criteria optimization is performed for the suggested system with net output power, energy efficiency, exergy efficiency, and system cost rate as objective functions. Besides, the multi-criteria decision analysis (MCDA) is also carried out on the obtained Pareto front using TOPSIS decision-maker to select the best operating condition that improves the output power, energy, and exergy efficiency by 52.6%, 49.6%, and 61.8%, respectively, at the expense of 5.2% increase in the system cost rate. The current investigation demonstrates how an appropriate optimized design of an integrated energy system using SGSP, PEMFC, and TEG can improve the overall performance with reasonable cost increment.

  • Salinity gradient solar pond;
  • PEM fuel Cell;
  • Waste heat recovery;

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