A thermoelectric generator has been proposed to be applied for waste heat of an incinerator without a damage of thermal stress  . However thermoelectric generating system has not been put into practical use yet because their cost, especially generating modules cost, is still high. In this paper a heat accumulator installed thermoelectric generating system for the batch operated incinerator was proposed and experimentally investigated. A heat accumulator has the potential to reduce cost of thermoelectric generating system by reduction of a capacity of employed thermoelectric generating modules. However optimal control of the thermoelectric generator attached with a heat accumulator has not been developed yet. The MPPT (Maximum Power Point Tracking) control accelerates the drop in the heat medium temperature by Peltier effect so that it cannot supply maximum electricity from heat stored in the heat accumulator. We proposed MEPT (Maximum Efficiency Point Tracking) control as an optimal control which electricity could be obtained from a heat accumulator more effectively than MPPT control.
2. Effect of a Heat Accumulator
2.1. Introduction of a Heat Accumulator into a Garbage Plant
In ordinary large scale garbage plants which dispose more than 200 [ton/day] combustible waste, conventional steam turbine generators are utilized for waste heat recovery. However a steam turbine generator is not applicable to a smaller scale garbage plant which is operated intermittently. Even in such cases thermoelectric generators can be applied. In this paper application of a thermoelectric generator for small scale garbage incinerator was studied. For design of thermoelectric generator it is necessary to estimate a capacity of thermoelectric generator. If all of heat generated in an incinerator is used for thermoelectric generation, generator capacity should amount to peak value of waste heat generation as shown Figure 1. However an excess of capacity of generator increase initial cost and generating cost. Therefore a heat accumulator which can deal with peak value of waste heat generation is effective to decrease initial cost and generating cost  .
As shown in Figure 2 a heat accumulator is proposed to be utilized for thermoelectric generation for heat recovery of waste heat in such incinerator so that the capacity of the thermoelectric generator and also the initial cost can be reduced. The excess waste heat which is more than the capacity of the thermoelectric generator is stored in the heat accumulator. The stored heat is used when
Figure 1. Hourly variation of waste heat generation.
Figure 2. Hourly variation of waste heat generation and heat transfer with an accumulator.
waste heat generation is smaller than the capacity of the thermoelectric generator.
2.2. Latent Heat Accumulator
There are two types of heat accumulators: sensible heat storage and latent heat storage. Latent heat storage employs PCM (Phase Change Material) as heat storage medium. A latent heat accumulator is more suitable for thermoelectric generation because stable operation temperature around melting point can help to achieve high conversion efficiency. Therefore the efficiency of thermoelectric generation is proportional to the temperature difference between heating medium and cooling medium. Table 1 shows properties of PCM of middle range of temperature. We employed KOH-NaOH eutectic mixture as heat storage material in our experiment. Melting point of KOH-NaOH is 170 degC suitable for employed thermoelectric generator and commercially available as industrial raw material.
3. Experimental Evaluation of Latent Heat Storage Thermoelectric Generation
3.1. Experimental Facilities
The experimental facility which consists of the heat accumulator which employs KOH-NaOH eutectic mixture, heat medium oil heating and circulating system which employs 25 kWe class electric heater, water cooler and 500 W class thermoelectric generator is schematically shown in Figure 3. The specifications of the employed thermoelectric generator are shown in Table 2.
The electric heater employed in heat medium oil heating and circulating system imitates waste heat generation. When the heater is switched off, heat stored in the heat accumulator is supplied as heat source of the thermoelectric generation for heat discharged mode.
Figure 4 shows the experimental results when inlet temperatures of heat medium oil and cooling water are 250 [degC] and 25 [degC] respectively, and flow rates of heat medium oil and cooling water and 18 [liter/m] and 20 [liter/m] respectively. For safety reason, the temperature and the flow rate of heat medium
Table 1. Properties of phase change material of intermediate-temperature   .
Table 2. Thermoelectric generator specification.
Figure 3. Experimental facilities.
oil are reduced from rated values. When the thermoelectric generator has the equivalent circuit that is connected the constant voltage source and the constant
Figure 4. Experimental results.
resistance, the Voltage-Current characteristics shows straight line and the Output-Current characteristics shows parabola. However as a result shown in Figure 4 V-I curve is not straight and P-I curve is not parabola. The peak area where the maximum power is obtained in P-I curve is slightly broad. This is because the properties of the modules connected in series and parallel vary according to temperature profile in the thermoelectric generator.
3.2. MPPT Control of a Thermoelectric Generator
Generally a thermoelectric generator is controlled by MPPT which is realized by hill climbing method. But current control based MPPT control employed for photovoltaic is not suitable for the large scale thermoelectric generator which has broad peak. This is because it is difficult to determine the adequate current control step which depends on temperature difference. So load resistance was proposed to be used for control parameter for MPPT control.
Figure 5 shows variation of MPPT controlled load resistance in variation of temperature of heat source. Load resistance is suitable for the MPPT control parameter because controlled load resistance fluctuates for almost same width in any heat source temperature as shown Figure 5. Load resistance controlled for maximum power increases from 3 [ohm] to 4 [ohm] when heat source temperature increases from 50 [degC] to 250 [degC].
3.3. Proposed Optimal Control of a Thermoelectric Generator
As mentioned above, even in the steady state operation, the control width is 10% of load resistance. When thermoelectric generator is operated by stored heat in discharged mode, controlled load resistance fluctuates more than 10%. In discharge mode heat source temperature decreases and it is more difficult to determine the maximum power point. Therefore, in such a case, an excess control to the lower load resistant causes significant increase of Peltier heat and acceleration of consumption of stored heat in the heat accumulator. For the reasons mentioned above it is reported that MPPT control cannot obtain the maximum electricity from limited energy stored in the heat accumulator.  Therefore we proposed MEPT (Maximum Efficiency Point Tracking) control to obtain the maximum electricity from limited energy. But when using limited energy stored in an accumulator heat source temperature is not constant and decrease gradually, so that it is difficult to determine the maximum efficiency point exactly.
Efficiency and power of the large scale thermoelectric generator was theoretically calculated as shown in Figure 6. This calculation is based on the condition that inlet temperatures of heat medium oil and cooling water are 220 [degC] and 25 [degC] respectively, and flow rates of heat medium oil and cooling water and 18 [liter/m] and 20 [liter/m] respectively.
Figure 6 shows that the current at the maximum efficiency point is 7.5 [A]. This is about 10% smaller than the current at the maximum power point. Therefore we proposed that maximum efficiency point should be determined as the point where the load resistance is 20% larger than the matching load.
3.4. Experimental Evaluation of MEPT Control
Proposed MEPT control was experimentally evaluated compared to MPPT control. Typical results are shown in Figure 7. A significant difference between MPPT control and MEPT control was not observed in their inlet temperatures. But obviously MEPT control exceeds MPPT control in recovered electrical
Figure 5. MPPT controlled load resistance.
Figure 6. Theoretical power and efficiency vs current.
Figure 7. Recovered electrical energy and inlet temperature vs current.
energy. During 1000 [sec] operation MPPT control and MPET control obtained 563 [kJ] and 607 [kJ] respectively.
In this study optimum control of a thermoelectric generator attached with a latent heat accumulator was proposed and experimentally evaluated. The obtained results are as follows:
1) Load resistance controlled for maximum power increases from 3 [ohm] to 4 [ohm] when heat source temperature increases from 50 [degC] to 250 [degC].
2) MEPT control current is 10% smaller than MPPT control current.
3) MEPT control exceeds MPPT control in recovered electrical energy.
 Kajikawa, T., et al. (1993) Conceptual Design of Thermoelectric Power Generation System Using the Waste Heat of Combustible Solid Waste. Proceedings of the 12th International Conference on Thermoelectrics, Yokohama, 7-10 November 1993, 491-496.
 Tsuyoshi, A., Michihira, M. and Kato, S. (2007) The Energy Recovery System of Unused Thermal Energy by Using the Thermoelectric Generator. IEEJ, Proceedings of 2017 IEE-Japan Industry Application Society Conference, 1-O7-1, Osaka, 20-22 August 2007, 137-140.