Next Article in Journal
Theoretical and Experimental Study on the Impact of Long-Wave Radiation on the Greenhouse Effect of a Prefabricated Temporary House
Next Article in Special Issue
Maximum Profit Output Configuration of Multi-Reservoir Resource Exchange Intermediary
Previous Article in Journal
Weighted Cumulative Past Extropy and Its Inference
Previous Article in Special Issue
Maximum Efficient Power Performance Analysis and Multi-Objective Optimization of Two-Stage Thermoelectric Generators
 
 
Font Type:
Arial Georgia Verdana
Font Size:
Aa Aa Aa
Line Spacing:
Column Width:
Background:
Article

Four-Objective Optimizations of a Single Resonance Energy Selective Electron Refrigerator

1
Institute of Thermal Science and Power Engineering, Wuhan Institute of Technology, Wuhan 430205, China
2
Hubei Provincial Engineering Technology Research Center of Green Chemical Equipment, Wuhan 430205, China
3
School of Mechanical & Electrical Engineering, Wuhan Institute of Technology, Wuhan 430205, China
*
Authors to whom correspondence should be addressed.
Entropy 2022, 24(10), 1445; https://doi.org/10.3390/e24101445
Submission received: 29 August 2022 / Revised: 20 September 2022 / Accepted: 5 October 2022 / Published: 11 October 2022

Abstract

:
According to the established model of a single resonance energy selective electron refrigerator with heat leakage in the previous literature, this paper performs multi-objective optimization with finite-time thermodynamic theory and NSGA-II algorithm. Cooling load ( R ¯ ), coefficient of performance ( ε ), ecological function ( E C O ¯ ), and figure of merit ( χ ¯ ) of the ESER are taken as objective functions. Energy boundary ( E / k B ) and resonance width ( Δ E / k B ) are regarded as optimization variables and their optimal intervals are obtained. The optimal solutions of quadru-, tri-, bi-, and single-objective optimizations are obtained by selecting the minimum deviation indices with three approaches of TOPSIS, LINMAP, and Shannon Entropy; the smaller the value of deviation index, the better the result. The results show that values of E / k B and Δ E / k B are closely related to the values of the four optimization objectives; selecting the appropriate values of the system can design the system for optimal performance. The deviation indices are 0.0812 with LINMAP and TOPSIS approaches for four-objective optimization ( E C O ¯ R ¯ ε χ ¯ ), while the deviation indices are 0.1085, 0.8455, 0.1865, and 0.1780 for four single-objective optimizations of maximum E C O ¯ , R ¯ , ε , and χ ¯ , respectively. Compared with single-objective optimization, four-objective optimization can better take different optimization objectives into account by choosing appropriate decision-making approaches. The optimal values of E / k B and Δ E / k B range mainly from 12 to 13, and 1.5 to 2.5, respectively, for the four-objective optimization.

1. Introduction

With the development of micro–nano technology, the micro energy conversion systems have gradually entered the field of view of modern thermodynamic researchers. As with motors in the macro world, there are also micro “motors” at the micro level, including quantum thermal cycles [1,2], Brownian motors [3,4], and electron engine systems [5,6,7], etc. They also function as motors in a mechanical sense; that is, they obtain mechanical energy by converting other forms of energy. In the studies on micro energy conversion systems, thermodynamic performance of the system has always been one of the core issues that people pay attention to. Due to their advantages of high efficiency, controllability, and easy integration, the optimal performance of these micro energy conversion systems has become a very active focus of modern thermodynamic research.
Since its establishment, the theory of finite time thermodynamics (FTT) [8,9,10,11,12,13,14,15,16,17,18,19] has been applied to research the optimal configurations [20,21,22,23,24,25,26,27,28,29,30,31,32,33,34,35,36,37,38,39,40,41,42,43] and the optimal performances [44,45,46,47,48,49,50,51,52,53,54,55,56,57,58,59,60,61,62,63,64,65,66,67,68,69,70,71,72,73,74,75,76,77] of thermal devices. The ideas of FTT considering performance optimization with heat leakage loss and finite rate heat transfer are also applicable to analyses and optimizations of micro energy conversion systems. Applying FTT to optimize micro energy conversion systems has not only achieved many research results of both theoretical significance and practical application value, but also broadened the application scope of the theory.
The model of an energy selective electron (ESE) heat engine was first established in 2002 [78], its working fluid constitutes electrons that are stored in two electron reservoirs and propagated through an energy filter. Electrons transfer under the influence of deflection voltage, temperature difference, and electrochemical potential difference. Since electrons carry energy, energy transfer also occurs during the transmission process, thereby realizing energy conversion.
In the research process of ESERs, in addition to the two basic performance indicators of cooling load (CL) and coefficient of performance (COP), there are also the figure of merit (FOM) [79,80,81] and ecological function [82,83,84]. Yan [79] first took the product of CL and COP as the optimization goal of the refrigerators in 1984; de Tomas et al. [80] named it as the FOM optimization criterion of the refrigerators and it was introduced into low-dissipation heat engines [81]. Angulo-Brown [82] first proposed the ecological function of heat engines in 1991 and it was defined as E = P T L σ , where P represents the power output, T L represents the temperature of the cold reservoir, and σ represents the entropy generation rate. Yan [83] thought that this ecological function did not inherently distinguish heat (energy) from work (exergy), and believed comparing exergy ( P ) and non-exergy ( T L σ ) was incomplete; then, he modified the ecological function to be E = P T 0 σ , where T 0 represents the environment temperature. Chen et al. [84] further proposed a unified ecological function for various thermodynamic cycles based on exergy and it was defined as E = A / τ T 0 σ , where A represents the exergy output and τ represents the cycle period. The ecological function and FOM can also take into account the COP and CL of the ESER. Humphrey [85] studied the COP and Cl performances of an endoreversible ESER, and Li et al. [86] studied its ecological function performance. When further considering heat leakage in ESERs, He et al. [87] studied the optimal performance of an irreversible ESER; Ding et al. [88] studied its optimal performance in two operating modes, and Zhou et al. [89] introduced the FOM and ecological function into it.
The performance optimizations mentioned above for ESERs are only aimed at a single optimization objective and there is usually only one optimal solution. With the increase of performance indicators, conflicts will occur among various indicators. In order to take different performance indicators into account and obtain the optimal design scheme, Deb et al. [90] proposed the non-dominated sorting genetic algorithm II (NSGA-II), which overcame the three shortcomings of NSGA, including the high computational complexity of non-dominated sorting, the lack of elite strategies, and the need to specify shared parameters. NSGA-II was widely used for the multi-objective optimization (MOO) of various thermodynamic cycles [91,92,93,94,95,96,97,98,99]. The Brayton cycle [91] and Stirling-Otto combined cycle [92] were optimized by MOO, and the utilized optimization objectives were power output and thermal efficiency; the optimization results were obtained and compared by applying different decision-making approaches. The porous-medium cycle [93] and Dual cycle [94] were optimized by MOO and the utilized optimization objectives were power density, power output, ecological function, and thermal efficiency; in addition, the effects of the compression ratio on four optimization objectives were analyzed. The Organic Rankine cycle [95] was optimized by applying MOO and its performances of pure and mixture working fluids were compared and studied. The ESE heat engine [96] was optimized by MOO and the utilized optimization objectives were ecological function, power output, efficient power, and thermal efficiency. Stirling engines [97,98], the membrane reactor [99], and the bidirectional-ribbed microchannel [100] were also optimized by applying MOO; and the schemes with less contradictions and conflicts were obtained.
There is no work concerning MOO for ESERs in open literature. On the basis of a model of a single resonance ESER with heat leakage established in Ref. [89], this paper will take resonance width and energy boundary as optimization variables to carry out MOO for the ESER with four objectives of CL, COP, FOM, and ecological function by applying the NSGA-II algorithm. The optimal design scheme will be obtained by comparing deviation indices of different optimization objectives combinations with LINMAP, TOPSIS, and Shannon Entropy (SE) approaches.

2. Model Description and Performance Indicators

Figure 1 gives a model of ESER with heat leakage [89]. It includes two electron reservoirs and an energy filter, which only allows electrons in a certain energy range to pass through. In the cold- and hot-electron reservoirs, the electrochemical potentials are μ C and μ H , and the temperatures are T C and T H , respectively. Δ E and E are important structural parameters of the energy filter, and they are the energy boundary and resonance width, respectively. According to Ref. [78], to make the ESE system work as an ESER, the value of the energy E of electrons involved in energy transfer must meet μ C < E < E 0 , where E 0 = ( μ C T H μ H T C ) / ( T H T C ) . During the working of the ESER, the heat transfer of electrons is irreversible due to the heat leakage loss caused by phonon propagation.
According to Refs. [78,85], in a small energy range, the heat transferred into hot-reservoir and from cold-reservoir are:
q ˙ H = 2 h ( E μ H ) ( f C f H ) δ E
q ˙ C = 2 h ( E μ C ) ( f C f H ) δ E
where h is Planck constant, and f C and f H are Fermi distributions of electrons:
f C = [ 1 + exp ( E μ C k B T C ) ] 1
f H = [ 1 + exp ( E μ H k B T H ) ] 1
where k B is Boltzmann constant.
From Equations (1)–(4), the total heat transferred into hot-reservoir ( Q ˙ H E ) and from cold-reservoir ( Q ˙ C E ) are
Q ˙ H E = 2 h E E + Δ E ( E μ H ) ( f C f H ) d E
Q ˙ C E = 2 h E E + Δ E ( E μ C ) ( f C f H ) d E
The heat leakage loss rate ( Q ˙ L ) caused by phonon propagation is
Q ˙ L = k L ( T H T C )
where k L is heat-leakage coefficient.
Combining Equations (5)–(7), the actual heats transferred into hot-reservoir ( Q ˙ H ) and from cold -reservoir ( Q ˙ C ) are
Q ˙ H = Q ˙ H E Q ˙ L
Q ˙ C = Q ˙ C E Q ˙ L
During the numerical solution, R H = E + Δ E μ H k B T H , r H = E μ H k B T H , R C = E + Δ E μ C k B T C and r C = E μ C k B T C are set, and Nielsen function g ( x ) = P o l y L o g ( 2 , x ) [101] is introduced.
From Equation (9), the CL ( R ) of the ESER can be obtained by
R = Q ˙ C = 2 h ( k B T C ) 2 [ 1 2 R C 2 g ( e ( R C ) ) R C ln ( 1 + e ( R C ) ) 1 2 r C 2 + g ( e ( r C ) ) + r c ln ( 1 + e ( r C ) ) ] 2 h ( k B T H ) 2 [ 1 2 R H 2 1 2 r H 2 R H ln ( 1 + e ( R H ) ) + r H ln ( 1 + e ( r H ) ) g ( e ( R H ) ) + g ( e ( r H ) ) ] + 2 h ( k B T H ) ( μ C μ H ) [ ln ( 1 + e ( r H ) ) ( 1 + e ( R H ) ) + R H r H ] k L ( T H T C )
From Equations (8)–(10), the COP ( ε ) can be expressed as
ε = R Q ˙ H Q ˙ C = { 2 h ( k B T C ) 2 [ 1 2 R C 2 + r C ln ( 1 + e ( r C ) ) + g ( e ( r C ) ) R C ln ( 1 + e ( R C ) ) g ( e ( R C ) ) 1 2 r C 2 ] 2 h ( k B T H ) 2 [ 1 2 R H 2 + r H ln ( 1 + e ( r H ) ) + g ( e ( r H ) ) 1 2 r H 2 R H ln ( 1 + e ( R H ) ) g ( e ( R H ) ) ] + 2 h k B T H ( μ C μ H ) [ R H + ln ( 1 + e ( r H ) ) ( 1 + e ( R H ) ) r H ] k L ( T H T C ) } / { 2 h k B [ T H ln 1 + e ( r H ) 1 + e ( R H ) T C ln 1 + e ( r C ) 1 + e ( R C ) ] ( μ H μ C ) }
Combining Equations (10) and (11), the FOM ( χ ) [79,80] can be given by
χ = R × ε = { 2 h ( k B T C ) 2 [ 1 2 R C 2 + r C ln ( 1 + e ( r C ) ) + g ( e ( r C ) ) R C ln ( 1 + e ( R C ) ) g ( e ( R C ) ) 1 2 r C 2 ] 2 h ( k B T H ) 2 [ 1 2 R H 2 + r H ln ( 1 + e ( r H ) ) + g ( e ( r H ) ) 1 2 r H 2 R H ln ( 1 + e ( R H ) ) g ( e ( R H ) ) ] + 2 h k B T H ( μ C μ H ) [ R H r H + ln ( 1 + e ( r H ) ) ( 1 + e ( R H ) ) ] k L ( T H T C ) } 2 / { 2 h k B [ T H ln 1 + e ( r H ) 1 + e ( R H ) T C ln 1 + e ( r C ) 1 + e ( R C ) ] ( μ H μ C ) }
For the ESER, entropy generation rate ( σ ) and exergy output rate ( A ) are, respectively
σ = Q ˙ H / T H Q ˙ C / T C
A = Q ˙ C ( T 0 / T C 1 ) Q ˙ H ( T 0 / T H 1 )
Combining Equations (13) and (14), and based on the definition formula of ecological function E C O = A T 0 σ [84], one has
E C O = 2 h k B ( μ H μ C ) [ T H ln 1 + e ( r H ) 1 + e ( R H ) T C ln 1 + e ( r C ) 1 + e ( R C ) ] 2 T 0 { 2 h k B 2 T C ( T H T C ) T H × [ g ( e ( r C ) ) g ( e ( R C ) ) + 1 2 R C 2 + r C ln ( 1 + e ( r C ) ) 1 2 r C 2 R C ln ( 1 + e ( R C ) ) ] 2 h k B 2 × T H ( T H T C ) T C [ 1 2 R H 2 + g ( e ( r H ) ) + r H ln ( 1 + e ( r H ) ) g ( e ( R H ) ) R H ln ( 1 + e ( R H ) ) 1 2 r H 2 ] + 2 h k B ( μ C μ H ) [ ( R C r C ) ( 1 T C T H ) + T H T C ln 1 + e ( r H ) 1 + e ( R H ) T C T H ln 1 + e ( r C ) 1 + e ( R C ) ] + ( T H T C ) 2 k L T H T C }
The dimensionless CL ( R ), FOM ( χ ), and ecological function ( E C O ¯ ) are defined as:
R ¯ = R / R max
χ ¯ = χ / χ max
E C O ¯ = E C O / E C O max

3. Multi-Objective Optimizations

In the MOO process, the solution set is not the only one, but a series of feasible alternatives; that is, the optimal solutions set in the multivariate space, which are called the “Pareto frontiers”. They are obtained by NSGA-II (see Figure 2 for flow chart). The steps of NSGA-II are: (1) the initialization population with size N is performed by non-dominated sorting; then, the first offspring population is obtained by selection, crossover, and variation through genetic algorithm; (2) in the second generation, merging the parent population and first offspring population for rapid non-dominated sorting, the crowding distance of individuals is calculated to select suitable individuals to form a new parent population; and (3) a new population of offspring is obtained with the genetic algorithm; when it meets the program requirements, the genetic algorithm will end and a Pareto optimal frontier will be obtained.
NSGA-II is an improvement for the shortcomings of NSGA, which can improve the convergence speed of the algorithm and maintain the diversity of results by adopting fast hierarchical sorting and elite strategies. In order to obtain an ideal design scheme by applying NSGA-II, three strategies including TOPSIS, LINMAP, and SE are usually adopted and their pros and cons are compared by deviation indices ( D s) obtained from them. The positive and negative ideal points are the solutions at which all performance indicators of Pareto frontiers reach the maximum and minimum values, respectively. TOPSIS strategy makes the solutions farthest from the negative ideal point, LINMAP strategy makes the solutions closest to positive ideal points, and SE strategy attains the solutions when the last performance indicator reaches its maximum.
The D represents the average distance between the solution and positive ideal point; the smaller the value, the better the result. The definition of D is
D = j = 1 m ( G j G j positive ) 2 j = 1 m ( G j G j positive ) 2 + j = 1 m ( G j G j negative ) 2
where G j is value of the j-th goal, G j positive is value of the j-th goal of positive ideal point, and G j negative is value of the j-th goal of negative ideal point.
According to Ref. [89], k L = 1.5 × 10 14   W / K , T 0 = 1.6   K , T C = 1.2   K , μ C / k B = 12   K , T H = 2.2   K and μ H / k B = 10   K are set. The value ranges of energy boundary E / k B and resonance width Δ E / k B are set to 10 ~ 15 and 0 ~ 5 , respectively.
Table 1 lists the setting parameters of NSGA-II. Table 2 gives the outcomes of various single-objective and multi-objective optimizations. From Table 2, the D s are 0.0812 with LINMAP and TOPSIS approaches when the MOO is performed on four-objective optimization ( E C O ¯ R ¯ ε χ ¯ ), while the D s are 0.1085, 0.8455, 0.1865, and 0.1780 for four single-objective optimizations of maximum E C O ¯ , R ¯ , ε , and χ ¯ , respectively. It indicates that compared with single-objective optimization, MOO can better take into account different optimization objectives by choosing appropriate decision-making methods. For the MOO of E C O ¯ R ¯ , the D obtained with the TOPSIS approach is 0.0809, which is the smallest and the most perfect scheme; and the corresponding values of the E / k B and Δ E / k B are 12.5887 and 1.8050, respectively.
Figure 3 gives the outcomes of different (six) bi-objective optimization combinations. It can be concluded from Figure 3 that two different performance indicators cannot achieve the best at the same time, and the improvement of one performance indicator will often lead to the deterioration of the other. From Figure 3 and Table 2, SE solutions represent the points when the performance indicators on the ordinate reach the maximum, LINMAP and TOPSIS solutions represent the points closest to the positive ideal point (1.0000, 1.0000, 0.4916, 1.0000) and the points farthest from the negative ideal point (−2.0171, 0.4739, 0.2943, 0.6532), respectively. As E C O ¯ grows, R ¯ , ε , and χ ¯ all decline. As R ¯ grows, both ε and χ ¯ decline. As ε grows, χ ¯ declines. From Table 2, for the MOOs of E C O ¯ ε and E C O ¯ χ ¯ , the D s (0.1229, 0.0884) obtained with the LINMAP approach are the same as those obtained with the TOPSIS approach, and are better than those obtained with the SE approach. For the MOOs of E C O ¯ R ¯ , R ¯ ε , and ε χ ¯ , the D s (0.0809, 0.3786, 0.0814) obtained with the TOPSIS approach are better than those obtained with LINMAP and SE approaches. For the MOO of R ¯ χ ¯ , the D (0.1780) obtained with SE is more perfect than that obtained with LINMAP and TOPSIS approaches.
Figure 4 gives the outcomes of different (four) tri-objective optimization combinations. As E C O ¯ grows, R ¯ declines, ε grows, and χ ¯ first grows and then declines. As R ¯ grows, ε declines, and χ ¯ first grows and then declines. From Table 2, for the MOO of E C O ¯ R ¯ ε , the D (0.0814) obtained with the LINMAP approach is the same as that obtained with the TOPSIS approach, and is better than that obtained with the SE approach. For the MOO of E C O ¯ R ¯ χ ¯ , the D (0.0816) obtained with the TOPSIS approach is better than that obtained with LINMAP and SE approaches. For the MOO of E C O ¯ ε χ ¯ and R ¯ ε χ ¯ , the D s (0.0888, 0.1692) obtained with the LINMAP approach are better than those obtained with TOPSIS and SE approaches.
Figure 5 gives the Pareto frontier for four-objective ( E C O ¯ R ¯ ε χ ¯ ) optimization. The numerical changes of R ¯ and ε are represented by three axes, and the numerical change of χ ¯ is represented by color change. The positive and negative points lie outside the Pareto frontier, which means that the four optimization objectives E C O ¯ , R ¯ , ε , and χ ¯ cannot be optimal or worst at the same time. As E C O ¯ grows, R ¯ declines, ε grows, and χ ¯ first grows and then declines. From Table 2, for the MOO of E C O ¯ R ¯ ε χ ¯ , the D s (0.0812, 0.0812) obtained with LINMAP and TOPSIS approaches are equal, which are more reasonable than those obtained with SE.
Figure 6 gives the distributions of ( E / k B ) o p t and ( Δ E / k B ) o p t obtained with four-objective optimization. In Figure 6a, the value of ( E / k B ) o p t ranges mainly from 12 to 13; as ( E / k B ) o p t grows, R ¯ continues to decline, ε continues to grow, E C O ¯ and χ ¯ grow first and then decline. From Figure 6b, the value of ( Δ E / k B ) o p t ranges mainly from 1.5 to 2.5; as ( Δ E / k B ) o p t grows, R ¯ continues to grow, ε continues to decline, E C O ¯ and χ ¯ grow first and then decline. From Figure 6, the values of E and Δ E are closely related to the values of the four optimization objectives ( E C O ¯ , R ¯ , ε and χ ¯ ), and the selection of the parameters of the energy filter is very important to improve the performance of ESERs.
Figure 7 and Figure 8 give the average distance and average spread in relation to generations obtained from two different MOOs. From the two figures, the genetic algorithm will end when it reaches convergence, which occurs at the 302th and 455th generations for four-objective ( E C O ¯ R ¯ ε χ ¯ ) and two-objective ( E C O ¯ R ¯ ) optimizations, respectively.

4. Conclusions

In this paper, according to the model established in Ref. [89], the NSGA-II is applied to perform MOO for a single resonance energy selective electron refrigerator with heat leakage. Four objective functions are introduced, including cooling load, coefficient of performance, figure of merit, and ecological function. The E and Δ E are regarded as optimization variables, their optimal intervals are obtained, and their effects on four objective functions are analyzed when the MOO is performed for E C O ¯ R ¯ ε χ ¯ . The results show that:
  • The D s obtained with LINMAP and TOPSIS approaches are 0.0812 for the MOO of E C O ¯ R ¯ ε χ ¯ , which are more reasonable than those obtained with the SE approach; at this time, the values of E / k B and Δ E / k B are 12.5958 and 1.8267, respectively. Comparing with the D s (0.1085, 0.8455, 0.1865, and 0.1780) for the four single-objective optimizations with maximum E C O ¯ , R ¯ , ε , and χ ¯ , the D s of the MOO are smaller. Therefore, compared with single-objective optimization, MOO can better take different optimization objectives into account by choosing appropriate decision-making methods.
  • When MOO is performed on E C O ¯ R ¯ , the D is the 0.0809 obtained with the TOPSIS approach, which is the closest point to the positive ideal point and the most reasonable solution; and the corresponding values of the E / k B and Δ E / k B are 12.5887 and 1.8050, respectively. When MOO is performed on other optimization objective combinations, the better solutions are obtained by choosing the appropriate decision-making approaches according to the design requirements.
  • For the MOO of E C O ¯ R ¯ ε χ ¯ , the value of ( E / k B ) o p t ranges mainly from 12 to 13; as ( E / k B ) o p t grows, R ¯ continues to decline, ε continues to grow, E C O ¯ and χ ¯ grow first and then decline. The value of ( Δ E / k B ) o p t ranges mainly from 1.5 to 2.5; as ( Δ E / k B ) o p t grows, R ¯ continues to grow, ε continues to decline, E C O ¯ and χ ¯ grow first and then decline. It indicates that the values of E and Δ E are closely related to values of the four optimization objectives ( E C O ¯ , R ¯ , ε , and χ ¯ ), and the selection of the parameters of the energy filter is very important to improve the performance of energy selective electron refrigerators.
  • For the MOO of E C O ¯ R ¯ ε χ ¯ and E C O ¯ R ¯ , the average distances range mainly from 0 to 0.5 and change slightly; the average spreads range mainly from 0 to 0.2, vary significantly before the 100th generations, and then remain stable.
  • NSGA-II and FTT theory are effective tools to guide the designs of energy selective electron refrigerators.

Author Contributions

Conceptualization: L.C. and F.L.; funding acquisition: L.C.; methodology: J.H.; software: J.H., Y.G. and S.S.; supervision: L.C., Y.G. and F.L.; validation: J.H., Y.G. and S.S.; writing—original draft preparation: J.H.; writing—reviewing and editing: L.C. All authors have read and agreed to the published version of the manuscript.

Funding

This work is supported by the National Natural Science Foundation of China (Project nos. 52171317 and 51779262) and Graduate Innovative Fund of Wuhan Institute of Technology (Project no. CX2021054).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Acknowledgments

The authors wish to thank the reviewers for their careful, unbiased, and constructive suggestions, which led to this revised manuscript.

Conflicts of Interest

The authors declare no conflict of interest.

Nomenclature

A Exergy output rate ( W )
E Energy boundary ( J )
E C O Ecological function
e V 0 Bias voltage
f Fermi distributions of electrons
g A defined function
h Plank constant ( J s )
k B Boltzmann constant ( J / K )
k L Heat leakage coefficient ( W / K )
Q Heat transfer ( W )
R Cooling load ( W )
Greek symbols
χ Figure of merit ( W )
ε Coefficient of performance
μ Electrochemical potential ( J )
σ Entropy generation rate ( W / K )
Δ E Resonance width ( J )
Subscripts
C Cold reservoir
C E Heat release rate
H Hot reservoir
H E Heat absorption rate
L Heat leakage
o p t Optimal
0 Environment
Superscripts
Dimensionless
Abbreviations
CLCooling load
COPCoefficient of performance
ESEREnergy selective electron refrigerator
FOMFigure of merit
FTTFinite time thermodynamics
MOOMulti-objective optimization
SEShannon Entropy

References

  1. Dann, R.; Kosloff, R.; Salamon, P. Quantum finite time thermodynamics: Insight from a single qubit engine. Entropy 2020, 22, 1255. [Google Scholar] [CrossRef] [PubMed]
  2. Purkait, C.; Biswas, A. Performance of Heisenberg-coupled spins as quantum Stirling heat machine near quantum critical point. Phys. Lett. A 2022, 442, 128180. [Google Scholar] [CrossRef]
  3. Zhang, Y.; Lin, B.H.; Chen, J.C. Performance characteristics of an irreversible thermally driven Brownian microscopic heat engine. Eur. Phys. J. B 2006, 53, 481–485. [Google Scholar] [CrossRef]
  4. Mamede, I.N.; Harunari, P.E.; Akasaki, B.; Proesmans, K. Obtaining efficient thermal engines from interacting Brownian particles under time-periodic drivings. Phys. Rev. E 2022, 105, 024106. [Google Scholar] [CrossRef]
  5. Peng, W.L.; Zhang, Y.C.; Yang, Z.M.; Chen, J.C. Performance evaluation and comparison of three-terminal energy selective electron devices with different connective ways and filter configurations. Eur. Phys. J. Plus 2018, 133, 38. [Google Scholar] [CrossRef]
  6. Lin, Z.B.; Yang, Y.Y.; Li, W.; Wang, J.H.; He, J.Z. Three-terminal refrigerator based on resonant-tunneling quantum wells. Phys. Rev. E 2020, 101, 22117. [Google Scholar] [CrossRef]
  7. Qiu, S.S.; Ding, Z.M.; Chen, L.G.; Ge, Y.L. Performance optimization of three-terminal energy selective electron generators. Sci. China Technol. Sci. 2021, 64, 1641–1652. [Google Scholar] [CrossRef]
  8. Moutier, J. Éléments de Thermodynamique; Gautier-Villars: Paris, France, 1872. [Google Scholar]
  9. Curzon, F.L.; Ahlborn, B. Efficiency of a Carnot engine at maximum power output. Am. J. Phys. 1975, 43, 22–24. [Google Scholar]
  10. Andresen, B. Finite-Time Thermodynamics; University of Copenhagen: Copenhagen, Denmark, 1983. [Google Scholar]
  11. Grazzini, G. Work from irreversible heat engines. Energy 1991, 16, 747–755. [Google Scholar] [CrossRef]
  12. Chen, L.G.; Wu, C.; Sun, F.R. Finite time thermodynamic optimization or entropy generation minimization of energy systems. J. Non-Equilib. Thermodyn. 1999, 24, 327–359. [Google Scholar]
  13. Feidt, M. Optimal thermodynamics-New upperbounds. Entropy 2009, 11, 529–547. [Google Scholar] [CrossRef]
  14. Andresen, B. Current trends in finite-time thermodynamics. Angew. Chem. Int. Ed. 2011, 50, 2690–2704. [Google Scholar] [CrossRef]
  15. Dumitrascu, G.; Feidt, M.; Popescu, A.; Grigorean, S. Endoreversible trigeneration cycle design based on finite physical dimensions thermodynamics. Energies 2019, 12, 3165. [Google Scholar]
  16. Abedinnezhad, S.; Ahmadi, M.H.; Pourkiaei, S.M.; Pourfayaz, F.; Mosavi, A.; Feidt, M.; Shamshirband, S. Thermodynamic assessment and multi-objective optimization of performance of irreversible Dual-Miller cycle. Energies 2019, 12, 4000. [Google Scholar] [CrossRef] [Green Version]
  17. Shittu, S.; Li, G.Q.; Zhao, X.D.; Ma, X.L. Review of thermoelectric geometry and structure optimization for performance enhancement. Appl. Energy 2020, 268, 115075. [Google Scholar] [CrossRef]
  18. Feidt, M.; Costea, M.; Feidt, R.; Danel, Q.; Périlhon, C. New criteria to characterize the waste heat recovery. Energies 2020, 13, 789. [Google Scholar] [CrossRef] [Green Version]
  19. Berry, R.S.; Salamon, P.; Andresen, B. How it all began. Entropy 2020, 22, 908. [Google Scholar] [CrossRef]
  20. Hoffman, K.H.; Burzler, J.; Fischer, A.; Schaller, M.; Schubert, S. Optimal process paths for endoreversible systems. J. Non-Equilib. Thermodyn. 2003, 28, 233–268. [Google Scholar] [CrossRef]
  21. Zaeva, M.A.; Tsirlin, A.M.; Didina, O.V. Finite time thermodynamics: Realizability domain of heat to work converters. J. Non-Equilib. Thermodyn. 2019, 44, 181–191. [Google Scholar] [CrossRef]
  22. Masser, R.; Hoffmann, K.H. Endoreversible modeling of a hydraulic recuperation system. Entropy 2020, 22, 383. [Google Scholar] [CrossRef] [Green Version]
  23. Kushner, A.; Lychagin, V.; Roop, M. Optimal thermodynamic processes for gases. Entropy 2020, 22, 448. [Google Scholar] [CrossRef]
  24. de Vos, A. Endoreversible models for the thermodynamics of computing. Entropy 2020, 22, 660. [Google Scholar] [CrossRef]
  25. Masser, R.; Khodja, A.; Scheunert, M.; Schwalbe, K.; Fischer, A.; Paul, R.; Hoffmann, K.H. Optimized piston motion for an alpha-type Stirling engine. Entropy 2020, 22, 700. [Google Scholar] [CrossRef]
  26. Tsirlin, A.; Gagarina, L. Finite-time thermodynamics in economics. Entropy 2020, 22, 891. [Google Scholar] [CrossRef]
  27. Tsirlin, A.; Sukin, I. Averaged optimization and finite-time thermodynamics. Entropy 2020, 22, 912. [Google Scholar] [CrossRef]
  28. Muschik, W.; Hoffmann, K.H. Modeling, simulation, and reconstruction of 2-reservoir heat-to-power processes in finite-time thermodynamics. Entropy 2020, 22, 997. [Google Scholar] [CrossRef]
  29. Insinga, A.R. The quantum friction and optimal finite-time performance of the quantum Otto cycle. Entropy 2020, 22, 1060. [Google Scholar] [CrossRef]
  30. Schön, J.C. Optimal control of hydrogen atom-like systems as thermodynamic engines in finite time. Entropy 2020, 22, 1066. [Google Scholar] [CrossRef]
  31. Andresen, B.; Essex, C. Thermodynamics at very long time and space scales. Entropy 2020, 22, 1090. [Google Scholar] [CrossRef]
  32. Scheunert, M.; Masser, R.; Khodja, A.; Paul, R.; Schwalbe, K.; Fischer, A.; Hoffmann, K.H. Power-optimized sinusoidal piston motion and its performance gain for an Alpha-type Stirling engine with limited regeneration. Energies 2020, 13, 4564. [Google Scholar] [CrossRef]
  33. Boikov, S.Y.; Andresen, B.; Akhremenkov, A.A.; Tsirlin, A.M. Evaluation of irreversibility and optimal organization of an integrated multi-stream heat exchange system. J. Non-Equilib. Thermodyn. 2020, 45, 155–171. [Google Scholar] [CrossRef]
  34. Li, J.F.; Guo, H.; Lei, B.; Wu, Y.T.; Ye, F.; Ma, C.F. An overview on subcritical organic Rankine cycle configurations with pure organic fluids. Int. J. Energy Res. 2021, 45, 12536–12563. [Google Scholar] [CrossRef]
  35. Wang, D.; Chen, H.; Wang, T.J.; Chen, Y.; Wei, J.Q. Study on configuration of gas-supercritical carbon dioxide combined cycle under different gas turbine power. Energy Rep. 2022, 8, 5965–5973. [Google Scholar] [CrossRef]
  36. Fu, T.; Du, J.Y.; Su, S.H.; Su, G.Z.; Chen, J.C. The optimum configuration design of a nanostructured thermoelectric device with resonance tunneling. Phys. Scr. 2022, 97, 055701. [Google Scholar] [CrossRef]
  37. Farhan, M.; Amjad, M.; Tahir, Z.U.T.; Anwar, Z.A.; Arslan, M.; Mujtaba, A.; Riaz, F.; Imran, S.; Razzaq, L.; Ali, M.; et al. Design and analysis of liquid cooling plates for different flow channel configurations. Therm. Sci. 2022, 26, 1463–1475. [Google Scholar] [CrossRef]
  38. Zhu, W.C.; Yang, W.L.; Yang, Y.; Li, Y.; Li, H.; Shi, Y.; Yang, Y.G.; Xie, C.J. Economic configuration optimization of onboard annual thermoelectric generators under multiple operating conditions. Renew. Energy 2022, 197, 486–499. [Google Scholar] [CrossRef]
  39. Chen, C.M.; Yang, S.; Pan, M.Q. Energy flow model analysis and configuration optimization of thermal management system. Heat Transf. Res. 2022, 53, 37–58. [Google Scholar] [CrossRef]
  40. Hussen, H.M.; Dhahad, H.A.; Alawee, W.H. Comparative exergy and energy analyses and optimization of different configurations for a laundry purpose. J. Therm. Eng. 2022, 8, 391–401. [Google Scholar] [CrossRef]
  41. Wolf, V.; Bertrand, A.; Leyer, S. Analysis of the thermodynamic performance of transcritical CO2 power cycle configurations for low grade waste heat recovery. Energy Rep. 2022, 8, 4196–4208. [Google Scholar] [CrossRef]
  42. Mikkelson, D.; Doster, J.M. Investigation of two concrete thermal energy storage system configurations for continuous power production. J. Energy Storage 2022, 51, 104387. [Google Scholar] [CrossRef]
  43. Li, P.L.; Chen, L.G.; Xia, S.J.; Kong, R.; Ge, Y.L. Total entropy generation rate minimization configuration of a membrane reactor of methanol synthesis via carbon dioxide hydrogenation. Sci. China Technol. Sci. 2022, 65, 657–678. [Google Scholar] [CrossRef]
  44. Hoffmann, K.H.; Burzler, J.M.; Schubert, S. Endoreversible thermodynamics. J. Non-Equilib. Thermodyn. 1997, 22, 311–355. [Google Scholar]
  45. Wagner, K.; Hoffmann, K.H. Endoreversible modeling of a PEM fuel cell. J. Non-Equilib. Thermodyn. 2015, 40, 283–294. [Google Scholar] [CrossRef]
  46. Muschik, W. Concepts of phenominological irreversible quantum thermodynamics I: Closed undecomposed Schottky systems in semi-classical description. J. Non-Equilib. Thermodyn. 2019, 44, 1–13. [Google Scholar] [CrossRef]
  47. Ponmurugan, M. Attainability of maximum work and the reversible efficiency of minimally nonlinear irreversible heat engines. J. Non-Equilib. Thermodyn. 2019, 44, 143–153. [Google Scholar] [CrossRef] [Green Version]
  48. Raman, R.; Kumar, N. Performance analysis of Diesel cycle under efficient power density condition with variable specific heat of working fluid. J. Non-Equilib. Thermodyn. 2019, 44, 405–416. [Google Scholar] [CrossRef]
  49. Schwalbe, K.; Hoffmann, K.H. Stochastic Novikov engine with Fourier heat transport. J. Non-Equilib. Thermodyn. 2019, 44, 417–424. [Google Scholar] [CrossRef]
  50. Morisaki, T.; Ikegami, Y. Maximum power of a multistage Rankine cycle in low-grade thermal energy conversion. Appl. Therm. Eng. 2014, 69, 78–85. [Google Scholar] [CrossRef]
  51. Yasunaga, T.; Ikegami, Y. Application of finite time thermodynamics for evaluation method of heat engines. Energy Procedia 2017, 129, 995–1001. [Google Scholar] [CrossRef]
  52. Yasunaga, T.; Fontaine, K.; Morisaki, T.; Ikegami, Y. Performance evaluation of heat exchangers for application to ocean thermal energy conversion system. Ocean Therm. Energy Convers. 2017, 22, 65–75. [Google Scholar]
  53. Yasunaga, T.; Koyama, N.; Noguchi, T.; Morisaki, T.; Ikegami, Y. Thermodynamical optimum heat source mean velocity in heat exchangers on OTEC. In Proceedings of the Grand Renewable Energy 2018 International Conference and Exhibition, Yokohama, Japan, 17–22 June 2018. [Google Scholar]
  54. Yasunaga, T.; Noguchi, T.; Morisaki, T.; Ikegami, Y. Basic heat exchanger performance evaluation method on OTEC. J. Mar. Sci. Eng. 2018, 6, 32. [Google Scholar] [CrossRef] [Green Version]
  55. Fontaine, K.; Yasunaga, T.; Ikegami, Y. OTEC maximum net power output using Carnot cycle and application to simplify heat exchanger selection. Entropy 2019, 21, 1143. [Google Scholar] [CrossRef] [Green Version]
  56. Yasunaga, T.; Ikegami, Y. Finite-time thermodynamic model for evaluating heat engines in ocean thermal energy conversion. Entropy 2020, 22, 211. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  57. Yasunaga, T.; Ikegami, Y. Fundamental characteristics in power generation by heat engines on ocean thermal energy conversion (Construction of finite-time thermodynamic model and effect of heat source flow rate). Trans. JSME, 2021; in press. (In Japanese) [Google Scholar]
  58. Feidt, M. Carnot cycle and heat engine: Fundamentals and applications. Entropy 2020, 22, 348. [Google Scholar] [CrossRef] [PubMed] [Green Version]
  59. Feidt, M.; Costea, M. Effect of machine entropy production on the optimal performance of a refrigerator. Entropy 2020, 22, 913. [Google Scholar] [CrossRef] [PubMed]
  60. Ma, Y.H. Effect of finite-size heat source’s heat capacity on the efficiency of heat engine. Entropy 2020, 22, 1002. [Google Scholar] [CrossRef] [PubMed]
  61. Rogolino, P.; Cimmelli, V.A. Thermoelectric efficiency of Silicon–Germanium alloys in finite-time thermodynamics. Entropy 2020, 22, 1116. [Google Scholar] [CrossRef] [PubMed]
  62. Levario-Medina, S.; Valencia-Ortega, G.; Barranco-Jimenez, M.A. Energetic optimization considering a generalization of the ecological criterion in traditional simple-cycle and combined cycle power plants. J. Non-Equilib. Thermodyn. 2020, 45, 269–290. [Google Scholar] [CrossRef]
  63. Diskin, D.; Tartakovsky, L. Efficiency at maximum power of the low-dissipation hybrid electrochemical-Otto cycle. Energies 2020, 13, 3961. [Google Scholar] [CrossRef]
  64. Zhu, S.B.; Jiao, G.Q.; Wang, J.H. Efficiency at maximum power of quantum-mechanical Carnot engine enhanced by energy quantization. Mod. Phys. Lett. B 2021, 35, 2150320. [Google Scholar] [CrossRef]
  65. Yasunaga, T.; Fontaine, K.; Ikegami, Y. Performance evaluation concept for ocean thermal energy conversion toward standardization and intelligent design. Energies 2021, 14, 2336. [Google Scholar] [CrossRef]
  66. Smith, Z.; Pal, P.S.; Deffner, S. Endoreversible Otto engines at maximal power. J. Non-Equilib. Thermodyn. 2020, 45, 305–310. [Google Scholar] [CrossRef]
  67. Badescu, V. Self-driven reverse thermal engines under monotonous and oscillatory optimal operation. J. Non-Equilib. Thermodyn. 2021, 46, 291–319. [Google Scholar]
  68. Zhang, X.; Yang, G.F.; Yan, M.Q.; Ang, L.K.; Ang, Y.S.; Chen, J.C. Design of an all-day electrical power generator based on thermoradiative devices. Sci. China Technol. Sci. 2021, 64, 2166–2173. [Google Scholar]
  69. Radzai, M.H.M.; Yaw, C.T.; Lim, C.W.; Koh, S.P.; Ahmad, N.A. Numerical analysis on the performance of a radiant cooling panel with serpentine-based design. Energies 2021, 14, 4744. [Google Scholar] [CrossRef]
  70. Valencia-Ortega, G.; Levario-Medina, S.; Barranco-Jiménez, M.A. The role of internal irreversibilities in the performance and stability of power plant models working at maximum ϵ-ecological function. J. Non-Equilib. Thermodyn. 2021, 46, 413–429. [Google Scholar]
  71. Lin, J.; Xie, S.; Jiang, C.X.; Sun, Y.F.; Chen, J.C.; Zhao, Y.R. Maximum power and corresponding efficiency of an irreversible blue heat engine for harnessing waste heat and salinity gradient energy. Sci. China Technol. Sci. 2022, 65, 646–656. [Google Scholar] [CrossRef]
  72. Badescu, V. Maximum work rate extractable from energy fluxes. J. Non-Equilib. Thermodyn. 2022, 47, 77–93. [Google Scholar]
  73. Paul, R.; Hoffmann, K.H. Optimizing the piston paths of Stirling cycle cryocoolers. J. Non-Equilib. Thermodyn. 2022, 47, 195–203. [Google Scholar]
  74. He, D.; Yu, Y.S.; Wang, C.J.; He, B.S. Maximum specific cycle net-work based performance analyses and optimizations of thermodynamic gas power cycles. Case Stud. Therm. Eng. 2022, 32, 101865. [Google Scholar]
  75. Liu, H.G.; He, J.Z.; Wang, J.H. Optimized finite-time performance of endoreversible quantum Carnot machine working with a squeezed bath. J. Appl. Phys. 2022, 131, 214303. [Google Scholar] [CrossRef]
  76. Gaikwad, V.P.; Mohite, S.S. Performance analysis of microchannel heat sink with flow disrupting pins. J. Therm. Eng. 2022, 8, 402–425. [Google Scholar] [CrossRef]
  77. Liu, X.; Zhang, C.F.; Zhou, J.G.; Xiong, X.; Wang, Y.P. Thermal performance of battery thermal management system using fins to enhance the combination of thermoelectric cooler and phase change material. Appl. Energy 2022, 322, 119503. [Google Scholar] [CrossRef]
  78. Humphrey, T.E.; Newbury, R.; Taylor, R.P.; Linke, H. Reversible quantum Brownian heat engines for electrons. Phys. Rev. Lett. 2002, 89, 11680. [Google Scholar] [CrossRef] [Green Version]
  79. Yan, Z.J. ε and R of a Carnot engine at maximum εR. Chin. J. Nat. 1984, 7, 73–74. (In Chinese) [Google Scholar]
  80. de Tomas, C.; Hernandez, A.C.; Roco, J.M.M. Optimal low symmetric dissipation Carnot engines and refrigerators. Phys. Rev. E 2012, 85, 010104. [Google Scholar] [CrossRef] [Green Version]
  81. Nilavarasi, K.; Ponmurugan, M. Optimized efficiency at maximum figure of merit and efficient power of power law dissipative Carnot like heat engines. J. Stat. Mech. Theory Exp. 2021, 4, 043208. [Google Scholar] [CrossRef]
  82. Angulo-Brown, F. An ecological optimization criterion for finite-time heat engines. J. Appl. Phys. 1991, 69, 7465–7469. [Google Scholar] [CrossRef]
  83. Yan, Z.J. Comment on “ecological optimization criterion for finite-time heat engines”. J. Appl. Phys. 1993, 73, 3583. [Google Scholar] [CrossRef] [Green Version]
  84. Chen, L.G.; Zhou, J.P.; Sun, F.R.; Wu, C. Ecological optimization for generalized irreversible Carnot engines. Appl. Energy 2004, 77, 327–338. [Google Scholar] [CrossRef]
  85. Humphrey, T.E. Mesoscopic Quantum Ratchets and the Thermodynamics of Energy Selective Electron Heat Engines. Ph.D. Thesis, University of New South Wales, Sydney, Australia, 2003. [Google Scholar]
  86. Li, C.; Li, R.W.; Luo, X.G.; He, J.Z. Performance characteristics and optimal analysis of an energy selective electron refrigerator. Int. J. Thermodyn. 2014, 17, 153–160. [Google Scholar]
  87. He, J.Z.; Wang, X.M.; Liang, H.N. Optimum performance analysis of an energy selective electron refrigerator affected by heat leaks. Phys. Scr. 2009, 80, 035701. [Google Scholar] [CrossRef]
  88. Ding, Z.M.; Chen, L.G.; Sun, F.R. Performance characteristic of energy selective electron (ESE) refrigerator with filter heat conduction. Rev. Mex. Fis. 2010, 56, 125–131. [Google Scholar]
  89. Zhou, J.L.; Chen, L.G.; Ding, Z.M.; Sun, F.R. Exploring the optimal performances of irreversible single resonance energy selective electron refrigerators. Eur. Phys. J. Plus 2016, 131, 149. [Google Scholar] [CrossRef]
  90. Deb, K.; Pratap, A.; Agarwal, S.; Meyarivan, T. A fast and elitist multiobjective genetic algorithm: NSGA-II. IEEE Trans. Evol. Comput. 2002, 6, 182–197. [Google Scholar]
  91. Arora, R.; Kaushik, S.C.; Kumar, R.; Arora, R. Soft computing based multi-objective optimization of Brayton cycle power plant with isothermal heat addition using evolutionary algorithm and decision making. Appl. Soft Comput. 2016, 46, 267–283. [Google Scholar]
  92. Ahmadi, M.H.; Ahmadi, M.A.; Pourfayaz, F.; Hosseinzade, H.; Acıkkalp, E.; Tlili, I.; Feidt, M. Designing a powered combined Otto and Stirling cycle power plant through multi-objective optimization approach. Renew. Sustain. Energy Rev. 2016, 62, 585–595. [Google Scholar] [CrossRef]
  93. Zang, P.C.; Chen, L.G.; Ge, Y.L.; Shi, S.S.; Feng, H.J. Four-objective optimization for an irreversible Porous Medium cycle with linear variation of working fluid’s specific heat. Entropy 2022, 24, 1074. [Google Scholar]
  94. Ge, Y.L.; Shi, S.S.; Chen, L.G.; Zhang, D.F.; Feng, H.J. Power density analysis and multi-objective optimization for an irreversible Dual cycle. J. Non-Equilib. Thermodyn. 2022, 47, 289–309. [Google Scholar] [CrossRef]
  95. Fergani, Z.; Morosuk, T.; Touil, D. Exergy-based multi-objective optimization of an organic Rankine cycle with a zeotropic mixture. Entropy 2021, 23, 954. [Google Scholar] [CrossRef]
  96. He, J.H.; Chen, L.G.; Ge, Y.L.; Shi, S.S.; Li, F. Multi-objective optimization of an irreversible single resonance energy-selective electron heat engine. Energies 2022, 24, 1074. [Google Scholar] [CrossRef]
  97. Rostami, M.; Assareh, E.; Moltames, R.; Jafarinejad, T. Thermo-economic analysis and multi-objective optimization of a solar dish Stirling engine. Energy Sources Part A 2021, 43, 2861–2877. [Google Scholar] [CrossRef]
  98. Ahmed, F.; Zhu, S.M.; Yu, G.Y.; Luo, E.C. A potent numerical model coupled with multi-objective NSGA-II algorithm for the optimal design of Stirling engine. Energy 2022, 247, 123468. [Google Scholar] [CrossRef]
  99. Chen, L.G.; Li, P.L.; Xia, S.J.; Kong, R.; Ge, Y.L. Multi-objective optimization of membrane reactor for steam methane reforming heated by molten salt. Sci. China Technol. Sci. 2022, 65, 1396–1414. [Google Scholar] [CrossRef]
  100. Wang, G.L.; Ding, G.F.; Liu, R.; Xie, D.D.; Wu, Y.J.; Miao, X.D. Multi-objective optimization of a bidirectional-ribbed microchannel based on CFD and NSGA-II genetic algorithm. Int. J. Therm. Sci. 2022, 181, 107731. [Google Scholar] [CrossRef]
  101. Luo, X.G.; He, J.Z.; Li, C.; Qiu, T. The impact of energy spectrum width in the energy selective electron low-temperature thermionic heat engine at maximum power. Phys. Lett. A 2013, 377, 1566–1570. [Google Scholar] [CrossRef]
Figure 1. Model of ESER with heat leakage [89].
Figure 1. Model of ESER with heat leakage [89].
Entropy 24 01445 g001
Figure 2. NSGA-II algorithm.
Figure 2. NSGA-II algorithm.
Entropy 24 01445 g002
Figure 3. Pareto frontiers for different two-objective optimizations.
Figure 3. Pareto frontiers for different two-objective optimizations.
Entropy 24 01445 g003aEntropy 24 01445 g003bEntropy 24 01445 g003c
Figure 4. Pareto frontiers for different three-objective optimizations.
Figure 4. Pareto frontiers for different three-objective optimizations.
Entropy 24 01445 g004aEntropy 24 01445 g004b
Figure 5. Pareto frontier for E C O ¯ R ¯ ε χ ¯ optimization.
Figure 5. Pareto frontier for E C O ¯ R ¯ ε χ ¯ optimization.
Entropy 24 01445 g005
Figure 6. Distributions of design variables in Pareto frontier.
Figure 6. Distributions of design variables in Pareto frontier.
Entropy 24 01445 g006
Figure 7. Average distance and average spread in relation to generations ( E C O ¯ R ¯ ε χ ¯ ).
Figure 7. Average distance and average spread in relation to generations ( E C O ¯ R ¯ ε χ ¯ ).
Entropy 24 01445 g007
Figure 8. Average distance and average spread in relation to generations ( E C O ¯ R ¯ ).
Figure 8. Average distance and average spread in relation to generations ( E C O ¯ R ¯ ).
Entropy 24 01445 g008
Table 1. Parameters of NSGA-II.
Table 1. Parameters of NSGA-II.
ParametersValue
Generations500
Population size300
Pareto fraction0.5
Crossover fraction0.8
Table 2. Outcomes of single-, bi-, tri-, and quadru-objective optimizations.
Table 2. Outcomes of single-, bi-, tri-, and quadru-objective optimizations.
Optimization MethodsDecision-
Making
Approaches
Optimization
Variables
Objective FunctionsDeviation
Index
E / k B Δ E / k B E C O ¯ R ¯ ε χ ¯ D
Quadru-objective optimization ( E C O ¯ , R ¯ , ε , and χ ¯ )LINMAP12.59581.82670.90360.76530.44670.95850.0812
TOPSIS12.59581.82670.90360.76530.44670.95850.0812
SE12.40421.99580.46870.88240.40421.00000.1780
Tri-objective
optimization
( E C O ¯ , R ¯ , and ε )
LINMAP12.57611.83050.87710.77870.44280.96690.0814
TOPSIS12.57611.83050.87710.77870.44280.96690.0814
SE12.98501.41490.82420.47250.49160.65120.1873
Tri-objective
optimization
( E C O ¯ , R ¯ , and χ ¯ )
LINMAP12.56991.81270.86730.78280.44150.96900.0821
TOPSIS12.57921.79160.88020.77630.44330.96500.0816
SE12.40421.99600.46870.88240.40421.00000.1780
Tri-objective
optimization
( E C O ¯ , ε , and χ ¯ )
LINMAP12.66241.74350.97020.71910.45920.92600.0888
TOPSIS12.67211.71410.97630.71210.46090.92020.0907
SE12.40421.99580.46870.88240.40421.00000.1780
Tri-objective
optimization
( R ¯ , ε , and χ ¯ )
LINMAP12.41301.98700.49750.87770.40630.99990.1692
TOPSIS12.39532.00530.43850.88710.40200.99990.1873
SE12.40411.99580.46850.88240.40421.00000.1781
Bi-objective
optimization
( E C O ¯ and R ¯ )
LINMAP12.57841.84200.87980.77710.44320.96570.0815
TOPSIS12.58871.80500.89510.77030.44540.96190.0809
SE11.99992.4007−2.01711.00000.29430.82510.8455
Bi-objective
optimization
( E C O ¯ and ε )
LINMAP12.80381.59680.98970.61410.48020.82680.1229
TOPSIS12.80381.59680.98970.61410.48020.82680.1229
SE12.98311.41690.82670.47390.49160.65330.1865
Bi-objective
optimization
( E C O ¯ and χ ¯ )
LINMAP12.66011.74760.96860.72070.45880.92720.0884
TOPSIS12.66011.74760.96860.72070.45880.92720.0884
SE12.40421.99590.46860.88240.40421.00000.1780
Bi-objective
optimization
( R ¯ and ε )
LINMAP12.41471.98490.50300.87680.40670.99990.5030
TOPSIS12.37852.02150.37860.89570.39790.99930.3786
SE12.98311.41680.82670.47390.49160.65320.8267
Bi-objective
optimization
( R ¯ and χ ¯ )
LINMAP12.22862.1564−0.31650.95940.35890.96550.4243
TOPSIS12.23912.1507−0.25780.95590.36170.96950.4059
SE12.40421.99580.46860.88240.40421.00000.1780
Bi-objective
optimization
( ε and χ ¯ )
LINMAP12.61841.80090.93070.74990.45110.94850.0824
TOPSIS12.60381.77660.91380.75990.44830.95520.0814
SE12.40411.99590.46850.88240.40421.00000.1781
Maximum E C O ¯ -12.75001.65001.00000.65490.47320.86900.1085
Maximum R ¯ -12.00002.4000−2.01711.00000.29430.82520.8455
Maximum ε -12.98321.41680.82670.47390.49160.65320.1865
Maximum χ ¯ -12.40421.99580.46870.88240.40421.00000.1780
Positive ideal point--1.00001.00000.49161.0000-
Negative ideal point--−2.01710.47390.29430.6532-
Publisher’s Note: MDPI stays neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Share and Cite

MDPI and ACS Style

He, J.; Chen, L.; Ge, Y.; Shi, S.; Li, F. Four-Objective Optimizations of a Single Resonance Energy Selective Electron Refrigerator. Entropy 2022, 24, 1445. https://doi.org/10.3390/e24101445

AMA Style

He J, Chen L, Ge Y, Shi S, Li F. Four-Objective Optimizations of a Single Resonance Energy Selective Electron Refrigerator. Entropy. 2022; 24(10):1445. https://doi.org/10.3390/e24101445

Chicago/Turabian Style

He, Jinhu, Lingen Chen, Yanlin Ge, Shuangshuang Shi, and Fang Li. 2022. "Four-Objective Optimizations of a Single Resonance Energy Selective Electron Refrigerator" Entropy 24, no. 10: 1445. https://doi.org/10.3390/e24101445

APA Style

He, J., Chen, L., Ge, Y., Shi, S., & Li, F. (2022). Four-Objective Optimizations of a Single Resonance Energy Selective Electron Refrigerator. Entropy, 24(10), 1445. https://doi.org/10.3390/e24101445

Note that from the first issue of 2016, this journal uses article numbers instead of page numbers. See further details here.

Article Metrics

Back to TopTop