Evaluation of Combined Heat and Power (CHP) Systems Using Fuzzy Shannon Entropy and Fuzzy TOPSIS
Abstract
:1. Introduction
- the conversion and efficient use of energy in all the sectors of the economy associated with a decline in energy intensity;
- the diversification of the energy mix towards renewable energy sources and technologies for energy conversion with low carbon emissions for electricity, heating and cooling;
- the decarbonization of transportation by shifting to alternative fuels;
- the complete liberalization and interconnection of energy systems using smart information and communication technologies to provide a flexible and interactive (customers/operators) service network.
2. Fuzzy Set Theory: Preliminaries
3. An Integrated Fuzzy Entropy and Fuzzy TOPSIS Approach
3.1. Shannon’s Entropy for Objective Weighting
3.2. Fuzzy Shannon’s Entropy Based on Αlpha-Cut
3.3. Fuzzy TOPSIS
4. Development of an Application for Ranking Combined Heat and Power (CHP) Technologies
4.1. Combined Heat and Power (CHP) Technologies
4.2. Algorithm and Results
- (1)
- Reciprocating engine: it is a well-known technology used in cars, trucks, construction equipment, marine propulsion and backup power applications and it can range in size from small hand equipment to power systems serving many homes. Reciprocating engines employ the expansion of hot gases to push a piston within a cylinder, converting the linear movement of the piston into power. The high level of maturity and low-cost reliability make this option very interesting for CHP application.
- (2)
- Steam turbine: this represents one of the most versatile and oldest prime mover technologies; in general, it is used to drive a generator or mechanical machinery. Steam turbines are well suited to medium- and large-scale industrial and institutional applications in which fuels, such as coal, biomass, various solid wastes and refinery residual oil, are available [86]. They can also be joined in a combined cycle using the waste heat from a gas turbine. In CHP applications, steam at lower pressure can be extracted from the turbine and used directly in industrial processes or for district heating or it can be employed to produce hot or chilled water [86]. For industrial applications, steam turbines are a simpler case of using CHP.
- (3)
- Gas turbine: this is an aeroderivative technology; indeed, it began to be used in aeroplane propulsion in the 1940s. Since 1990, this technology has been employed for power only generation or in combined heat and power (CHP) systems in stationary applications in many countries of the world. In many cases, gas turbines are utilized by utilities to cover the energy demand peak. Gas turbines, available in sizes ranging from 150 kW to 250 MW, produce high-quality exhaust heat that can be used in CHP layout to reach overall efficiencies (electricity and thermal energy) of 70%–80% [87]. This makes gas turbines very attractive for CHP applications.
- (4)
- Microturbine: this is an electricity generator that burns gaseous and liquid fuels that can be used in power-only generation or in CHP systems to produce both electricity and heat on a small scale. The microturbine technology was originally based on the truck turbocharger technology that exploits the energy in engine exhaust heat [88]. The size range is from 30 to 300 kW and they are able to operate with several fuels and, in (CHP) applications, they may take an increasing share of this market, offering more benefits compared with other technologies for small-scale power generation [89]. Microturbines are mechanically simple and very compact. Their small size and low weight per unit of power lead to reduced engineering costs, while the small number of moving parts produces less noise [90].
- (5)
- Fuel cells: these are electrochemical systems capable of converting chemical energy of a fuel (generally hydrogen) directly into electricity without any direct combustion and intermediate thermal cycle. Since the fuel is not combusted, fuel cells offer a clean and efficient power generation system with very minimal air pollution. In CHP applications, the recovered heat depends on the type of fuel cell and its operating temperature. The parameters determining the performance of the fuel cell are dependent on the electrolyte material and composition of the membrane electrode assembly MEA [91]. The relationship of the materials to the performance of the device is significant and many important contributions in this topic can be found in the literature [92,93,94,95,96,97]. There are several kinds of fuel cells classified on the basis of the electrochemical process utilized. The principal types include: alkaline (AFC), polimer electrolyte (PEFC), phosphoric acid (PAFC), molten carbonate (MCFC) solid oxide (SOFC) and direct methanol (DMFC).
- (C1)
- Electric efficiency. This is defined as the ratio of the electric power output and the input power. In general it differs by technology and by size: larger systems are usually more efficient than smaller systems.
- (C2)
- Overall CHP efficiency. This expresses the energy content of both electricity and steam. It represents the net electrical power output plus the net thermal output (of the CHP system) divided by the fuel consumed.
- (C3)
- Fuel utilization. This measures the CHP efficiency as the ratio of net electrical output to net fuel consumption, in which the net fuel consumption does not include the share of fuel that produces the heat output.
- (C4)
- Power to heat ratio. This specifies the quantity of power (electrical or mechanical) to heat energy created in the CHP system.
- (C5)
- Installed costs. This criterion includes the costs of the equipment installation, project management, engineering and interest. Larger-capacity CHP systems in general have lower installed costs than smaller capacity systems.
- (C6)
- O&M costs. These include all the costs relating to the plant, employees’ wages, materials and installations, preventive maintenance transport and hire charges. As with capital costs, also the O&M costs tend to be reduced for larger systems.
- (C7)
- GHG reduction. Because in CHP systems less fuel is combusted, greenhouse gas emissions such as carbon dioxide (CO2) and other air pollutants are decreased. This criterion expresses the avoided GHG emissions due to the CHP system.
- Step 4.1: transform fuzzy data (Table 1) into interval data based on the alpha-cut using Equation (13);
- Step 4.2: normalize the interval (alpha cut = 0.1, 0.5, 0.9) decision matrix according to Equations (15) and (16) (Table 2);
- Step 4.3: calculate the lower bound and the upper bound of the interval entropy by Equations (17) and (18);
- Step 4.4: compute the degree of diversification and using Equations (19) and (20);
- Step 4.5: finally, by applying Equations (21) and (22), we obtain the lower and upper bounds of the interval weight, as shown in Table 3.
5. Conclusions
Acknowledgments
Author Contributions
Conflicts of Interest
References
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C1 | C2 | C3 | C4 | C5 | C6 | C7 | ||
---|---|---|---|---|---|---|---|---|
Electric Efficiency (%) | Overall CHP Efficiency (%) | Fuel Utilization (%) | Power to Heat Ratio (%) | Installed Costs ($/kWe) | O&M Costs ($/kWhe) | GHG Reduction (%) | ||
A1 | Recip. engine | (27,34,41) | (77,78.5,80) | (75,77.5,80) | (0.5,0.85,1.2) | (1500,2200,2900) | (0.009,0.017,0.025) | (31.50,35,38.5) |
A2 | Steam turbine | (5,17.5,30) | (70,75,80) | (75,76,77) | (0.07,0.085,0.1) | (670,885,1100) | (0.006,0.008,0.01) | (38.70,43,47.3) |
A3 | Gas turbine | (24,30,36) | (66,68.5,71) | (50,56,62) | (0.6,0.85,1.1) | (1200,2250,3000) | (0.006,0.00095,0.13) | (41.40,46,50.6) |
A4 | Microturbine | (22,29,36) | (63,66.5,70) | (49,53,57) | (0.5,0.6,0.7) | (2500,3400,4300) | (0.009,0.011,0.13) | (47.70,53,58.3) |
A5 | Fuel cell | (30,46.5,63) | (55,67.5,80) | (55,67.5,80) | (1,1.5,2) | (5000,5750,6500) | (0.032,0.035,0.038) | (50.40,56,61.6) |
C1 | C2 | C3 | C4 | C5 | C6 | C7 | ||
---|---|---|---|---|---|---|---|---|
Electric Efficiency (%) | Overall CHP Efficiency (%) | Fuel Utilization (%) | Power to Heat Ratio (%) | Installed Costs ($/kWe) | O&M Costs ($/kWhe) | GHG reduction (%) | ||
α = 0.1 | ||||||||
A1 | Recip. engine | [0.143,0.208] | [0.204,0.211] | [0.213,0.226] | [0.107,0.234] | [0.090,0.162] | [0.101,0.249] | [0.125,0.150] |
A2 | Steam turbine | [0.032,0.149] | [0.186,0.210] | [0.213,0.218] | [0.014,0.020] | [0.040,0.062] | [0.064,0.101] | [0.154,0.185] |
A3 | Gas turbine | [0.127,0.183] | [0.175,0.187] | [0.143,0.174] | [0.126,0.216] | [0.074,0.167] | [0.065,0.130] | [0.165,0.197] |
A4 | Microturbine | [0.115,0.143] | [0.167,0.184] | [0.140,0.160] | [0.102,0.139] | [0.148,0.241] | [0.095,0.132] | [0.190,0.227] |
A5 | Fuel cell | [0.164,0.317] | [0.149,0.208] | [0.159,0.223] | [0.211,0.392] | [0.291,0.368] | [0.332,0.388] | [0.201,0.240] |
α = 0.5 | ||||||||
A1 | Recip. engine | [0.174,0.214] | [0.211,0.215] | [0.222,0.230] | [0.150,0.228] | [0.115,0.159] | [0.145,0234] | [0.136,0.150] |
A2 | Steam turbine | [0.064,0.135] | [0.197,0.210] | [0.220,0.223] | [0.017,0.021] | [0.048,0.062] | [0.078,0.100] | [0.167,0.185] |
A3 | Gas turbine | [0.154,0.188] | [0.182,0.189] | [0.155,0.172] | [0.161,0.217] | [0.103,0.159] | [0.086,0.125] | [0.179,0.197] |
A4 | Microturbine | [0.134,0.151] | [0.176,0.185] | [0.149,0.160] | [0.122,0.145] | [0.184,0.240] | [0.111,0.134] | [0.206,0.227] |
A5 | Fuel cell | [0.218,0.312] | [0.166,0.200] | [0.179,0.215] | [0.278,0.390] | [0.335,0.381] | [0.373,0.407] | [0.217,0.240] |
α = 0.9 | ||||||||
A1 | Recip. engine | [0.211,0.220] | [0.219,0.219] | [0.232,0.234] | [0.203,0.221] | [0.145,0.155] | [0.197,0.216] | [0.147,0.150] |
A2 | Steam turbine | [0.103,0.119] | [0.208,0.211] | [0.228,0.229] | [0.021,0.022] | [0.059,0.062] | [0.095,0.100] | [0.181,0.185] |
A3 | Gas turbine | [0.187,0.194] | [0.190,0.192] | [0.167,0.170] | [0.206,0.218] | [0.137,0.149] | [0.111,0.120] | [0.194,0.197] |
A4 | Microturbine | [0.157,0.161] | [0.185,0.186] | [0.158,0.161] | [0.147,0.152] | [0.225,0.238] | [0.131,0.136] | [0.223,0.227] |
A5 | Fuel cell | [0.285,0.306] | [0.185,0.192] | [0.199,0.207] | [0.362,0.387] | [0.387,0.397] | [0.421,0.429] | [0.236,0.240] |
Α = 0.1 | Α = 0.5 | Α = 0.9 | |||||||
---|---|---|---|---|---|---|---|---|---|
C1 | 0.022 | 0.743 | 0.38 | 0.033 | 0.420 | 0.23 | 0.065 | 0.142 | 0.10 |
C2 | 0.001 | 0.152 | 0.08 | 0.001 | 0.082 | 0.04 | 0.003 | 0.018 | 0.01 |
C3 | 0.005 | 0.189 | 0.10 | 0.007 | 0.109 | 0.06 | 0.015 | 0.036 | 0.03 |
C4 | 0.106 | 0.876 | 0.49 | 0.155 | 0.607 | 0.38 | 0.275 | 0.383 | 0.33 |
C5 | 0.064 | 0.774 | 0.42 | 0.104 | 0.530 | 0.32 | 0.209 | 0.313 | 0.14 |
C6 | 0.063 | 0.783 | 0.42 | 0.104 | 0.537 | 0.32 | 0.213 | 0.320 | 0.27 |
C7 | 0.006 | 0.227 | 0.12 | 0.009 | 0.130 | 0.07 | 0.017 | 0.042 | 0.03 |
Α = 0.1 | Α = 0.5 | Α = 0.9 | ||||||||||
---|---|---|---|---|---|---|---|---|---|---|---|---|
d+ | d− | Cci | Rank | d+ | d− | Cci | Rank | d+ | d− | Cci | Rank | |
A1 | 6.043 | 1.001 | 0.142 | 4 | 6.345 | 0.686 | 0.098 | 4 | 6.558 | 0.467 | 0.066 | 4 |
A2 | 5.975 | 1.066 | 0.151 | 2 | 6.281 | 0.744 | 0.106 | 2 | 6.490 | 0.526 | 0.075 | 2 |
A3 | 5.950 | 1.095 | 0.155 | 1 | 6.267 | 0.764 | 0.109 | 1 | 6.484 | 0.541 | 0.077 | 1 |
A4 | 6.151 | 0.858 | 0.122 | 5 | 6.419 | 0.587 | 0.084 | 5 | 6.607 | 0.398 | 0.057 | 5 |
A5 | 5.987 | 1.053 | 0.150 | 3 | 6.312 | 0.712 | 0.101 | 3 | 6.546 | 0.470 | 0.067 | 3 |
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Cavallaro, F.; Zavadskas, E.K.; Raslanas, S. Evaluation of Combined Heat and Power (CHP) Systems Using Fuzzy Shannon Entropy and Fuzzy TOPSIS. Sustainability 2016, 8, 556. https://doi.org/10.3390/su8060556
Cavallaro F, Zavadskas EK, Raslanas S. Evaluation of Combined Heat and Power (CHP) Systems Using Fuzzy Shannon Entropy and Fuzzy TOPSIS. Sustainability. 2016; 8(6):556. https://doi.org/10.3390/su8060556
Chicago/Turabian StyleCavallaro, Fausto, Edmundas Kazimieras Zavadskas, and Saulius Raslanas. 2016. "Evaluation of Combined Heat and Power (CHP) Systems Using Fuzzy Shannon Entropy and Fuzzy TOPSIS" Sustainability 8, no. 6: 556. https://doi.org/10.3390/su8060556
APA StyleCavallaro, F., Zavadskas, E. K., & Raslanas, S. (2016). Evaluation of Combined Heat and Power (CHP) Systems Using Fuzzy Shannon Entropy and Fuzzy TOPSIS. Sustainability, 8(6), 556. https://doi.org/10.3390/su8060556