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[ Original Paper ] | |
Journal of Advanced Marine Engineering and Technology - Vol. 45, No. 6, pp. 339-344 | |
Abbreviation: JAMET | |
ISSN: 2234-7925 (Print) 2765-4796 (Online) | |
Print publication date 31 Dec 2021 | |
Received 17 Jul 2021 Revised 21 Jul 2021 Accepted 29 Nov 2021 | |
DOI: https://doi.org/10.5916/jamet.2021.45.6.339 | |
Study on the fundamental thermal analysis of thermoelectric generator systems | |
1Ph. D., Head Office of Kunsan University, Kunsan Natioinal University, Tel: +82-63-469-8990 (jiksuyu@kunsan.ac.kr) | |
Correspondence to : †Professor, Division of Marine Engineering, Kunsan National University, 558, Daehak-ro, Gunsan-si, Jeollabuk-do 54150, Korea, E-mail: mjkim@kunsan.ac.kr, Tel: +82-63-469-1849 | |
Copyright © The Korean Society of Marine Engineering This is an Open Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/by-nc/3.0), which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited. | |
Funding Information ▼ |
This study investigates the temperature characteristics and efficiency of a Peltier element for waste heat recovery from a ship. The Peltier element is calculated using its heat balance and performance. The results are as follows: 1) In the case of gas and water as the heat source, the temperature profile estimated from the performance and heat balance of the Peltier element generated deviations. 2) In the case of gas and water as the heat source, the thermoelectric scale effect changed the heat transfer rate considered between the heat source and the Peltier element existed. 3) In the case of water as the heat source, the thermoelectric scale effect changed the heat transfer rate considered between the heat source and the Peltier element did not exist.
Keywords: Waste heat, Thermoelectric generation, Peltier element, Scale effect, Heat transfer rate |
The world is making various efforts to reduce greenhouse gas (GHG) emissions, the main culprits of global warming. The Republic of Korea, the world’s seventh largest emitter of GHGs, aims to reduce GHG emissions by 37 % compared to “business as usual” by 2030 according to the Paris Climate Agreement. Measures such as the conversion from fossil fuels to new and renewable energies are being considered as a way to reduce GHG emissions. However, efforts in each industry and alternative energy resources to existing fossil fuels are required to achieve the 2030 GHG emissions reduction goal.
Recently, research on energy conversion has been conducted to recover renewable energy, such as waste heat, from industrial processes. Among the research on energy conversion, thermoelectric power generation using the Peltier element is being studied because this element is small and simple. Moreover, research related to thermoelectric power generation is actively being conducted [1][2].
Thermoelectric power generation generates electricity from heat using the “Seebeck effect,” which generates a voltage when there is a temperature difference between two different types of metals or semiconductors, and directly recovers waste heat as electrical energy without using other fossil fuels. It is a material technology that best responds to GHG reduction policies through energy saving [3]. Thermoelectric device technology is widely applied in automobiles, aerospace/aviation, semiconductors, optics, computers, power generation, and home appliances [4][5][6]. To apply these technologies to various fields and increase the efficiency of the systems, research is being conducted in research institutes and companies; however, research applied to ships is insufficient.
The purpose of this study is to incorporate a thermoelectric power generation system on a ship to recover the waste heat given off as exhaust gas from the ship. In addition, we intend to understand the temperature distribution and efficiency inside the system by considering the heat balance between the heat source and the thermoelectric element. Calculations are performed using MathCad Prime 3.0 in the engineering tools.
Table 1 lists the conditions of the heat source, and Table 2 lists the specifications of the thermoelectric element. To simplify the analysis, it is assumed that the properties of the Peltier element do not depend on temperature.
Define of heat source | At the hot side | At the cold side | |
---|---|---|---|
Heat transfer medium | Exhaust gas | Used coolant of lubricant | Coolant |
Temperature, °C | 300 | 80 | 20 |
Mechanism of heat transfer | Forced Convection | ||
Film coefficient of heat transfer, W/m2K | 50 | 6,000 | 6,000 |
Quality of plumbing | Stainless | ||
Thickness of plumbing, m | 0.01 | ||
Thermal conductivity, W/mK | 16.5 | ||
Overall heat transfer coefficient, W/m2K | 48.5 | 1,290 | 1,290 |
Country of Manufacture | Japan | |
---|---|---|
Maker | Kyocera | |
Model No. | 40×40 Module | |
Item | Unit | Value |
Length | mm | 40 |
Width | mm | 40 |
Area, S | mm2 | 1600 |
Thickness | mm | 2.3 |
Temperature at the hot side, Thj | °C | 20 |
Temperature difference, ΔTj | °C | 67 |
Temperature at the cold side, Tcj | °C | -47 |
Average temperature, (Thj + Tcj)/2 | °C | -13.5 |
Seebeck coefficient, α | V/K | 4.836×10-3 |
Internal resistance, Ri | Ω | 1.900 |
Internal resistance rate, ρi | Ωm | 1.322 |
Internal heat conductance, K | W/K | 4.908×10-3 |
Internal thermal conductivity, λi | W/mK | 7.055×10-3 |
Thermoelectric figure of merit, Z | 1/K | 2.508×10-3 |
Figure 1 shows the thermal analysis model. The heat balance between the Peltier element and the heat source is calculated following the procedure detailed by the conventional research of an author [7] as follows:
(1) |
Module | Unit | Single | Serial | Parallel | Serial+Parallel |
---|---|---|---|---|---|
Number | ea | 1 | m | n | m×n |
Seebeck coefficient | W/K | α | mα | α | mα |
Interal resistance | Ω | R | mR | R/n | (m/n)R |
Heat conductance | W/K | K | mK | nK | mnK |
CASE 1 | CASE 2 | CASE 3 | CASE 4 | |
---|---|---|---|---|
Connection | Serial | Serial × Parallel | ||
Number of devices | 4 | 16(4×4) | ||
Heat source at high temperature | Exhaust gas | Cooling water from the low temperature part |
Exhaust gas | Cooling water from the low temperature part |
The current I is calculated from the electromotive force V, as shown in Equation (2).
(2) |
(3) |
(4) |
(5) |
(6) |
Here, the coefficients F1, F2, F3, and F4 in Equation (6) are obtained using the following equations:
(7) |
Here, the coefficients F5, F6, and F7 are obtained by the following equations:
(8) |
The analysis results for CASE 1 are shown in Figure 3. The result of the performance of the Peltier element is the initial calculated value obtained in ② of Section 3, and the result of the heat balance shows the value calculated over ⑦ to ⑨ of Section 3.
When checking the temperature difference between the heat source and the thermoelectric element from the value calculated by the heat balance, it can be seen that a difference of 0.61 °C on the low-temperature side and of 47.17 °C on the high-temperature side occurred. The reason for this temperature difference was considered to affect the temperature distribution by a phenomenon in which the overall heat transfer coefficient on the high-temperature side is significantly lower than the value on the low-temperature side.
The analysis results for CASE 2 are shown in Figure 4. Unlike CASE 1, it can be seen that the temperature difference between the thermoelectric element and the heat source did not occur in both the high- and low-temperature sides. This result indicated that the total heat transfer coefficient of the high-temperature side increased to a greater extent than that of CASE 1, and there was little difference in the total heat transfer coefficient of the low-temperature side.
To confirm the effect of increasing the scale of the system, a calculation was performed when the number of thermoelectric elements was increased from four to 16 (four in series × four in parallel) without changing the heat source under the condition of CASE 1.
The results are shown in Figure 5.
Compared to the results of CASE 1, the results of the Peltier element performance showed that the temperature difference between the thermoelectric elements changed from ⁓200 °C to ⁓110 °C. In addition, as a result of the heat balance, it was confirmed that the temperature difference between the thermoelectric elements decreased from ⁓200 °C to ⁓110 °C.
Looking at the result calculated from the heat balance, the temperature difference between the heat source and the thermoelectric element was ⁓6.8 °C on the low-temperature side and ⁓161.5 °C on the high-temperature side. That is, by increasing the thermoelectric element, the temperature difference between the heat source and the thermoelectric element on the low-temperature side decreased, while the temperature difference between the heat source and the thermoelectric element on the high-temperature side increased. Notably, the difference in the overall heat transfer coefficient affected the temperature distribution.
In general, the thermoelectric conversion system is widely known because one of its advantages is that it does not affect scale-up/down. In this case, it can be considered that the effect of scale-up existed owing to the influence of the overall heat transfer coefficient of the high- and low-temperature sides.
Under the same conditions as in CASE 2, the result of the calculation by increasing the number of thermoelectric elements from four to 16 (four in series × four in parallel) without changing the heat source is shown in Figure 6.
Comparing the results of CASES 4 and 2, it can be seen that the temperature distribution and temperature at each point were almost the same. From this result, it can be considered that there was little effect of increasing the number of thermoelectric elements. This was considered to be because the overall heat transfer coefficient on the high-temperature side and the cooling side was sufficiently high.
Figure 7 shows the system efficiency of each CASE. First, if we check the results calculated with the heat balances of CASES 1 and 3, the efficiency was approximately 9–7 %.
However, it should be noted that the voltage or current of the thermoelectric element in this case was calculated using the values from the performance of the Peltier element. The efficiency in this case was 4–8 %.
The maximum efficiency of CASES 2 and 4, where both the hot and cold heat sources were liquid, was ~2.7 %. Because the overall heat transfer coefficient was sufficiently high on the high-temperature side and the cooling side, it can be seen that the temperature distribution or efficiency did not change significantly even if the scale of the thermoelectric generator system was increased.
Meanwhile, for CASES 1 and 3, the efficiency was expected to increase further by increasing the overall heat transfer coefficient of the exhaust gas side. However, because this was related to the pressure loss of the exhaust gas side, more reviews are expected.
In this study, to introduce a thermoelectric power generation system in a ship, the following results were derived by setting the specifications of the heat source and thermoelectric element, and estimating the temperature distribution inside the system considering the heat balance between the heat source and thermoelectric element.
The author wishes to acknowledge the financial support of the Fisheries Science Institute of Kunsan National University
Conceptualization, J. S. Yu and M. J. Kim; Methodology, J. S. Yu; Software, J. S. Yu; Validation, J. S. Yu and M. J. Kim; Formal Analysis, J. S. Yu; Investigation, J. S. Yu; Resources, J. S. Yu; Data Curation, J. S. Yu; Writing—Original Draft Preparation, J. S. Yu; Writing—Review & Editing, M. J. Kim; Visualization, J. S. Yu; Supervision, M. J. Kim; Project Administration, M. J. Kim; Funding Acquisition, M. J. Kim.
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