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Proceedings of ECOS 2009 22 nd International Conference on Efficiency, Cost, Optimization<br />

Copyright © 2009 by ABCM Simulation and Environmental Impact of Energy Systems<br />

August 31 – September 3, 2009, Foz do Iguaçu, Paraná, Brazil<br />

<strong>APPLYING</strong> <strong><strong>THE</strong>RMOECONOMICS</strong> <strong>TO</strong> <strong>THE</strong> <strong>ANALYSIS</strong> <strong>OF</strong> <strong>THE</strong> NORTH<br />

AMERICAN FOOD CHAIN<br />

César Torres Cuadra, cesar.torres@endesa.es<br />

Antonio Valero Capilla, valero@unizar.es<br />

Alicia Valero Delgado, aliciavd@unizar.es<br />

Maryori Díaz Ramírez, mdiaz@unizar.es<br />

CIRCE – Centro de Investigación de Recursos y Consumos Energéticos<br />

Centro Politécnico Superior University of Zaragoza, SPAIN<br />

Abstract. Thermoeconomic analysis is used to understand the process of cost formation and how to improve the design<br />

and the operation of extensive energy consumption systems such as power and chemical plants.<br />

This paper shows the capabilities for using the thermoeconomic analysis in environmental systems, and demonstrates<br />

that it could become a useful tool for identifying the ways for improving the energy resources cost and the efficiency of<br />

a macroeconomic system such as the American food chain. The environmental impact associated to each process in the<br />

food chain can be quantified through a thermoeconomic approach as a cost function, which represents the required<br />

natural resources to obtain a final product. Symbolic exergoeconomics is used to quantify the environmental impact of<br />

the food system. In the example, the fuel-product model is built and several simulations such as the impact of the<br />

change of meat diet basis by a vegetable diet, and reusing the residual biomass are analyzed.<br />

Keywords: Thermoeconomics, food chain, environmental systems.<br />

1. INTRODUCTION<br />

The earth is increasing naturally its entropy and the economic advance is accelerating the process because the<br />

economic process degrades natural resources and pollutes the environment (Georgescu-Roegen, 1971).<br />

Thermoeconomic analysis combines economic and thermodynamic analysis by applying the Second Law Analysis.<br />

The physical entity connecting thermodynamics and economics is the entropy generation or irreversibility. It represents<br />

the useful energy destroyed in all physical processes. Since all common processes in the actual industrial systems are<br />

not reversible, natural resources are consumed and lost forever. The more irreversible a process is the more natural<br />

resources are consumed. Nothing can be done without the expenditure of natural resources, and the amount of natural<br />

resources required to obtain a “desired” product is equivalent to its thermodynamic cost. All the production processes<br />

are irreversible. Consequently, the thermodynamic cost of a product can be also expressed as the “useful” energy<br />

contained in the product plus all the irreversibilities generated to obtain it (Torres et al., 2008). The analysis of the cost<br />

formation of processes is where physics best connects with economics.<br />

Thermoeconomic analysis normally uses exergy as the measure of the usefulness of the energy contained in the<br />

production flows. The exergy of a flow is the minimum amount of work required for its production, from the<br />

environment reference, and it lets to formulate the equivalence between different matter and/or energy streams of an<br />

energy system.<br />

Thermoeconomics is a general theory for energy saving (Lozano et al. 1993), which has been commonly used in the<br />

analysis of power or chemical plants, see for example the CGAM (Valero et al. 1992) or the TADEUS (Valero et al.,<br />

2002) works.<br />

The aim of this paper is to explain how thermoeconomics can be applied to a wider variety of energy and<br />

environmental systems. To illustrate their capabilities we will use as an example the analysis of the North American<br />

food chain.<br />

The methodology presented here is closely related to the input/output analysis (ten Raa, 2005), the mathematical<br />

principles are very similar, but in the Fuel-Product model, the Second Law is used in the analysis of the economic<br />

processes. Furthermore, it could be also connected to Life Cycle Analysis in general and to exergetic lifeycle analysis in<br />

particular (Cornelissen, 1997).<br />

In the traditional societies before 20 th century the ratio between required energy in agriculture and provided energy<br />

in form of food was 1:100, hence their products took mainly their energy from the solar radiation absorbed by plants.<br />

However, nowadays modern agriculture requires much more energy than the calories we consume in form of food. For<br />

example, for industrialized beef production using animal feed from overseas the ratio is 35:1, and it may reach extreme<br />

values of 500:1 for winter greenhouse vegetables (von Weizsacker et al. 1998).<br />

Besides the CO2 coming from the fossil fuel use, agriculture production increases the atmosphere’s carbon stock<br />

through forest clearing and the release of soil carbon through crop growing. Food production also contributes to global<br />

warming through the release of methane from livestock, crop and the burning of residuals (Deumling, D. et al., 2003).<br />

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Every human activity has an environmental impact, with the food system being an important (and mandatory)<br />

human activity. There is a wide variation in environmental impact according to the type of food, and the method of<br />

producing the food. An important feedback principle links the environment and food systems. The environment<br />

influences the quality and capacity of food production, which in turn influences the environment. A degraded<br />

environment may be less healthy for humans and other organisms, and also less able to produce the range and amount<br />

of food that an environment in better condition could achieve (Riley, M., 2005). Each basic process that comprises the<br />

food chain has an efficiency and a resources cost that could be evaluated by means of the thermoeconomic analysis,<br />

allowing the identification of improving options.<br />

2. <strong>THE</strong> FUEL –PRODUCT MODEL<br />

Symbolic Exergoeconomics (Torres, 2004) provides general relationships between the production demand and the<br />

resources cost with the efficiency and irreversibilities of the individual process of an energy system. It is based on the<br />

productive structure of the system and is represented by the fuel – product table, (fig. 1) which describes how the<br />

production processes are related.<br />

F0 F1 … Fn<br />

P0 E01 … E0n<br />

P1 E10 E11 … E1n<br />

… … … Eij …<br />

Pn En0 E1n … Enn<br />

Figure 1. Generic Fuel-Product Table<br />

In this table, the useful energy carried from the i-th process to the j-th process is represented as E ij . The sum of each<br />

row of the table is the production of each process, and the sum of each column is the resources or fuel required for each<br />

process.<br />

Symbolic exergoeconomic provides two different representations of the productive model:<br />

The FP representation allows relating the production and the cost of each process of the system as a function of:<br />

F ≡ E , … E<br />

• The external resources ( )<br />

e 10 n0<br />

• The efficiency of each process, represented by K D , a diagonal matrix whose elements are the unit<br />

•<br />

consumption of each process: κi ≡ Fi / Pi<br />

.<br />

The distribution ratios, represented by FP , a matrix whose elements are defined as yij ≡ EjiPj. The production of each process is obtained as:<br />

( ) 1<br />

P =〈 P| Fe The total production demand is calculated as:<br />

where 〈 P| = KD− −<br />

FP (1)<br />

t<br />

P T = y0P F e<br />

(2)<br />

y ( , , ) is a vector that contains the distribution ratios related to the environment.<br />

t<br />

where 0 ≡ y01 … y0n<br />

The production cost of each process is given by:<br />

*<br />

CP=〈 P | C0where *<br />

〈 P | = ( UD−<br />

−1<br />

FP )<br />

(3)<br />

the vector C0 ≡ ( c01E01, …, c0nE0n) contains the cost of the external resources and c 0i represents its unitary cost. The<br />

magnitude used to measure the external resources determines the type of cost obtained.<br />

The other representation, called PF representation, allows expressing the resources and their costs as a function of:<br />

• The production demand P s ≡ ( E10, …,<br />

En0)<br />

• The efficiency of each process i i / i F P ≡ ε<br />

• The junction ratios, represented by PF , a matriz which elements are defined as qij ≡ Eij/ Fi<br />

The resources used in each process are obtained as:<br />

( ) 1<br />

F = F Pswhere 〈 F | = HD−<br />

−<br />

PF (4)<br />

−1<br />

and HD ≡ K D is a diagonal matrix (n× n), containing the efficiency ε i of each process.<br />

The cost per production unit can be obtained as:<br />

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Proceedings of ECOS 2009 22 nd International Conference on Efficiency, Cost, Optimization<br />

Copyright © 2009 by ABCM Simulation and Environmental Impact of Energy Systems<br />

August 31 – September 3, 2009, Foz do Iguaçu, Paraná, Brazil<br />

t<br />

P<br />

where cˆ0i ≡ c0iq0, i.<br />

The total cost of the external resources 0<br />

c = F c ˆ<br />

(5)<br />

0<br />

0<br />

C can be expressed as a function of the system demand as:<br />

t<br />

C = cˆ F P (6)<br />

Using these relationships is it also possible to determine the variation of the total resources as a function of the<br />

variation of the parameters of the PF representation:<br />

n ⎛ ⎞<br />

Δ C0 = ∑⎜c0iΔ q0 iFi + ∑ cP, jΔ qjiFi + cF, iΔ<br />

κiPi<br />

+ cP, iΔEi0⎟ (7)<br />

i=<br />

1 ⎝ j<br />

⎠<br />

The above expression is known as the Fuel Impact Formulae (Torres et al., 2002), the first two terms correspond to<br />

the variation of the junction (structural) ratios, the third term to the variation of the processes efficiency and the last<br />

term to the system demand variation.<br />

Through the example presented in the next section, we will show how thermoeconomics can be applied to a<br />

macroeconomic system such as the American food chain, giving insights on improving options.<br />

3. <strong>APPLYING</strong> <strong><strong>THE</strong>RMOECONOMICS</strong> <strong>TO</strong> <strong>THE</strong> <strong>ANALYSIS</strong> <strong>OF</strong> <strong>THE</strong> FOOD CHAIN<br />

The Global 2000 Report (Barney, 1980) presented a flow diagram of energy for American food production (see<br />

figure 2). For around 3.6 GJ (per capita) of human food energy, 35.5 GJ of technical energy are expended, without<br />

accounting for the “solar gift” of 80 GJ that is absorbed by the plants used in the process. It seems more than plausible<br />

that the energy demand from agriculture and food processing could be substantially reduced with essentially no<br />

sacrifice of wellbeing (Weizsacker, 1997). And thermoeconomics could help to identify and quantify these reductions.<br />

According to the diagram of figure 2, the food chain system could be decomposed into five basic processes,<br />

represented in the productive diagram of figure 3.<br />

80 60<br />

1 2<br />

(1) Vegetal biomass production<br />

(2) Harvest production<br />

(3) Animal food production<br />

(4) Vegetal food production<br />

(5) Human food demand<br />

7<br />

0<br />

51.5<br />

5<br />

3.5<br />

s<br />

15<br />

3<br />

4<br />

13.5<br />

Figure 3. Productive diagram of the food chain in the USA<br />

3.1. The base food chain<br />

The thermoeconomic model of the base food chain of Fig. 3 is represented by the following Fuel-Product table.<br />

From this table it is possible to obtain the production cost of each process. In this example we are interested to separate<br />

the cost associated to fossil fuels and the cost associated to biomass energy, because the saving of these resources has a<br />

different interpretation. Fossil fuels are required in all processes of food production: draining, irrigation, chemical<br />

products, mechanical manufacturing, cattle raising, food preparation, shipping and distribution…, whereas biomass<br />

energy is provided by the plants, taking energy from the sun.<br />

889<br />

1.9<br />

3.1<br />

5<br />

3.6


Table 1. Fuel-Product Table of the food chain (GJ)<br />

0 F 1 F 2 F 3 F 4<br />

F 5<br />

F Total<br />

P0 80 7 15 13.5 0 115.5<br />

P1 0 0 60 0 0 0 60<br />

P2 5 0 0 51.5 3.5 0 60<br />

P3 0 0 0 0 0 1.9 1.9<br />

P4 0 0 0 0 0 3.1 3.1<br />

P5 3.6 0 0 0 0 0 3.6<br />

Total 8.6 80 67 66.5 17 5<br />

Equations (3) and (5) allow computing the production cost. These equations could be also used to decompose the<br />

costs considering the different types of resources. The resource cost vector can be separated into two parts:<br />

fossil biomass<br />

fossil<br />

C0 = C0 + C 0 , where the cost due to fossil fuels in terms of energy resources is C 0 = (0, E02, E03, E04,0)<br />

, and<br />

biomass<br />

the cost due to biomass is C 0 = ( E01,0,0,0,0)<br />

, therefore the production cost due to fossil fuel could be computed as:<br />

fossil<br />

CP= *<br />

P<br />

fossil<br />

C0<br />

(8)<br />

and in the same way the production cost due to biomass is:<br />

biomass<br />

CP= *<br />

P<br />

biomass<br />

C0<br />

(9)<br />

Similar expressions could be used to compute the unitary production cost.<br />

Table 2. Efficiency and production costs of the processes for the base case<br />

Fossil Fuels Biomass Total<br />

Process κ P c (GJ/GJ) P C (GJ) P c (GJ/GJ) P C (GJ) P c (GJ/GJ) C P (GJ)<br />

1 1.33 0.00 0.00 1.33 80.00 1.33 80.00<br />

2 1.12 0.12 7.00 1.33 80.00 1.45 87.00<br />

3 35.00 11.06 21.01 36.14 68.67 47.20 89.68<br />

4 5.48 4.49 13.91 1.51 4.67 5.99 18.58<br />

5 1.39 9.70 34.92 20.37 73.33 30.07 108.25<br />

Total 13.43 35.50 80.00 115.50<br />

In table 2 the efficiency values of each system process are shown. The ratio of the total fossil fuel required per<br />

fossil<br />

calorie consumed is approximately 10:1 ( c P,5<br />

= 9.70 ), a clear indicator of the high inefficiency of the current food<br />

chain. Also note that the production of meat (process 3) requires 2.5 times more fossil energy resources (11.06 vs. 4.49)<br />

than the vegetal production (process 4). By far, the most inefficient process (identified by κ ) is the production of meat.<br />

Starting with the base case we will analyze several scenarios, in order to demonstrate the capabilities of the<br />

thermoeconomic approach for the evaluation of the environmental impact of the food system, and for the identification<br />

of potential improvements.<br />

3.2 Recycling biomass residues<br />

Our aim now is to identify and quantify possible optimization options of the food chain system. In the first scenario,<br />

we are going to analyze the effect of recycling 10% of crop residues (2 GJ) and reusing them as fuel in the next process.<br />

The unit consumption of the first process is reduced to κ 1 = 1.29 and the external resources of the second process to<br />

C 02 = 5. We assume that the distribution ratios and the final demand of the system do not change.<br />

Using Eqn. (3) it is possible to compute the production costs. Since biomass energy and the cost distribution matrix<br />

*<br />

P does not change, the production costs due to biomass do not change either.<br />

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Proceedings of ECOS 2009 22 nd International Conference on Efficiency, Cost, Optimization<br />

Copyright © 2009 by ABCM Simulation and Environmental Impact of Energy Systems<br />

August 31 – September 3, 2009, Foz do Iguaçu, Paraná, Brazil<br />

Table 3. Production costs due to fossil fuel, recycling 10% biomass<br />

Fossil Fuels<br />

Process P c (GJ/GJ) C P (GJ)<br />

1 0 0<br />

2 0.08 5<br />

3 10.15 19.29<br />

4 4.45 13.79<br />

5 9.19 33.08<br />

Total 33.50<br />

Table 3 shows the new costs due to fossil fuels. As it can be seen, recycling 10% of crop residues reduces the fuel<br />

consumption by 2 GJ, or what is the same, the ratio between the fuel required and the energy consumption is reduced by<br />

5.25%.<br />

3.3. Process efficiency impact<br />

In this scenario we will assume that the efficiency of each single process is increased by 10% without modifying<br />

the final demand and the system structure (junction ratios). Eqn (7) is used for this purpose, with Δ κi<br />

= 0.1.<br />

The impact<br />

in resources consumption is decomposed into the part coming from biomass and from fossil fuels (see table 4).<br />

Table 4. Impact of resources consumption with a 10% increase on the process efficiency<br />

Process 0 C Δ Fossil Fuels (GJ) 0 C Δ Biomass (GJ) 0 C<br />

Δ Total (GJ)<br />

1 0.000 0.00% 6.000 7.50% 6.000 5.19%<br />

2 0.627 1.77% 7.881 9.85% 8.507 7.37%<br />

3 0.060 0.17% 0.216 0.27% 0.276 0.24%<br />

4 0.254 0.71% 0.094 0.12% 0.347 0.30%<br />

5 2.514 7.08% 5.808 7.26% 8.322 7.21%<br />

Eqn. (10) is used to compute the fuel impact of each efficiency simulation. The cost of fuel is evaluated for the<br />

simulated scenario and the production corresponds to the base case.<br />

i<br />

0<br />

Δ C0 = cF, iΔ κi<br />

Pi<br />

(10)<br />

Note that improving the efficiency of the last stage of the food chain has an important impact on the fossil fuel<br />

consumption. On the other hand improving the efficiency of the first stages of the process has an impact only on the<br />

reduction of biomass requirements. An important conclusion can be thus drawn: for improving the energy efficiency of<br />

the food chain, major efforts should be focused on the last production stages.<br />

3.4. Change in the food diet<br />

The last scenario analyzes a change in the diet. As it has been shown, the production of animal food requires much<br />

more resources than vegetable food. In the base model a person consumes 62% of vegetables and 38% of animal food.<br />

What would happen if we reduced the consumption of meat by 10% maintaining the final demand of energy per person<br />

in 3.6 GJ?<br />

To simulate this scenario we must change the junction ratios q 35 = 0,38 → 0,318 and q 45 = 0.62 → 0.682 . The rest<br />

of the parameters are kept constant. Eqn. (7) can be used to compute the resources consumption impact for this<br />

simulation as:<br />

Δ C0 = ( cP,3Δ q35 + cP, 4Δ q45) F5<br />

(11)<br />

Using Eqn. (11) with the unit production cost due to fossil fuel and biomass, the change implies a saving of 10.74<br />

GJ (13.42 %) of biomass resources, and 2.04 GJ (5.73 %) of fossil fuels.<br />

On the other hand, if we would reduce the energy demand per person by 10%, the associated saving would be equal<br />

to 3.49 GJ (9.84%) of fossil fuels and 7.33 GJ (9.16 %) of biomass, which could be computed using the expression:<br />

Δ C0 = cP, 5Δ E50<br />

(12)<br />

In these simulations we have differentiated between fossil fuel and biomass resources. The first one has an explicit<br />

cost: it has a market price, an environmental impact, externality costs, etc. The second one is a different case, since<br />

biomass energy is provided by the sun which is “free”. Nevertheless, the solar energy provided to biomass is<br />

proportional to the harvest area. Furthermore in this model we are considering the energy consumed per habitant,<br />

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therefore a reduction of biomass resources implies a reduction of required harvest area, or what is the same, more<br />

people could be fed with the same land. Hence, the reduction of biomass requirements per habitant is also a key point in<br />

sustainable developing.<br />

4. CONCLUSIONS<br />

Symbolic thermoeconomics is a general methodology for the thermoeconomic analysis of exergy systems. Its main<br />

objective is the analysis of the cost formation process in energy systems and its interaction with the environment.<br />

The environmental impact associated to each process of the food chain system can be quantified as a cost function,<br />

in terms of natural resources consumption. This example illustrates the capabilities of thermoeconomic analysis to be<br />

applied to macroeconomic environmental systems. In this kind of systems with a high level of aggregation, it is<br />

possible to use as free variables the efficiency of the process or the structural junction ratios. However, in microsystems<br />

such as power plants with a high level of dissagregation, these parameters are mutually dependent.<br />

In the analysis made in this paper it is shown that an animal-based diet requires more energy, land and other natural<br />

resources than a plant-based diet. In fact, the production and processing of meat (and other animal products) has the<br />

largest impact on energy use, water use and land disturbance of all our various consumption activities. A soft change in<br />

the human diet, consuming less meat and supplying the required energy demand with a richer vegetal diet, provides an<br />

important fossil fuel saving and allows feeding more people. Other aspects of thermoeconomics such as the principle of<br />

non-equivalence of the irreversibilities (Kotas, 1984) are also illustrated in this example, showing the importance of<br />

reducing and recycling wastes and improving the efficiency of the last stages of the productive food chain. An<br />

improvement of the food processing can be accomplished by buying locally grown and seasonal products, reducing the<br />

fossil fuel consumption.<br />

The search of a sustainable food system will generate benefits in numerous areas: health, biodiversity, ecological<br />

restoration, energy saving or economic justice. None of these benefits alone may outweigh the apparent sort term gains<br />

of the current destructive system. But the sum of these benefits will make a more sustainable society and will help to<br />

avoid the trap of increasing production and entropy generation at the expense of a more and more degraded earth.<br />

REFERENCES<br />

Barney, G.O., 1980. “The Global 2000 Report to the President of the US. Entering the 21st Century,Vol. 1. The<br />

Summary Report” . Pergamon Press, NewYork.<br />

Cornelissen, R.L., 1997 “Thermodynamics and sustainable development; the use of exergy analysis and the reduction of<br />

irreversibility” Ph.D. Thesis, University of Twente, Enschede, The Netherlands, available at:<br />

http://doc.utwente.nl/32030<br />

Deumling, D., Wackernagel, M., and Monfreda, Ch., 2003, “Eating up the earth: how sustainable food systems shrink<br />

our ecological footprint”, Agriculture Footprint Brief, Redefining Progress, available at:<br />

http://www.rprogress.org/newpubs/2003/ag_food_0703.pdf<br />

Georgescu-Roegen N., 1971. “The Entropy Law and the Economic Process”. Harvard University Press.<br />

Kotas, T. J., 1985 “The exergy Method of Thermal Plant Analysis” Butterworths.<br />

Lozano M.A and Valero A., 1993 “Theory of exergetic cost”. Energy vol.18(9), pp. 939-960<br />

Raa, T., 2005 “The Economics of Input-Output Analysis”. Cambridge University Press.<br />

Riley, M. , 2005. “Eating green: How should we eat to best protect the environment”, available at:<br />

http://www.heia.com.au/heia_graphics/JHEIA12-1-6.pdf<br />

Torres, C., Valero, A. Serra L. And Royo, J. 2002. “Structural theory and thermoeconomic diagnosis: Part I. On<br />

malfunction and dysfunction analysis”. Energy Conversion and Management, Vol. 43, pp. 1503-1518<br />

Torres, C., 2004. “Symbolic Thermoeconomic Analysis of Energy Systems”. In Exergy, Energy System Analysis and<br />

Optimization, edited by Christos A. Frangopoulos. In Encyclopaedia of Life Support Systems (EOLSS), Developed<br />

under the Auspices of the UNESCO, Eolss Publishers, Oxford, UK. http://www.eolss.net.<br />

von Weizsacker, E. Lovins, A. and Lovins, L., 1997. Factor Four: Doubling Wealth, Halving Resource Use.- The New<br />

Report to the Club of Rome. Earthscan Ltd.<br />

Valero A., Lozano M.A., Serra L., Tsatsaronis, G., Pisa J., Frangopoulos C.A., and von Spakovsy M.R., 1994. “CGAM<br />

problem: Definition and conventional solution”. Energy vol.19. pp. 279–286.<br />

Valero A., et al., 2004. “On the thermoeconomic approach to the diagnosis of energy system malfunctions Part 1: The<br />

TADEUS problem”. Energy vol. 29, pp. 1875-1887.<br />

RESPONSIBILITY NOTICE<br />

The authors are the only responsibles for the printed material included in this paper.<br />

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Proceedings of ECOS 2009 22 nd International Conference on Efficiency, Cost, Optimization<br />

Copyright © 2009 by ABCM Simulation and Environmental Impact of Energy Systems<br />

August 31 – September 3, 2009, Foz do Iguaçu, Paraná, Brazil<br />

Figure 2. Energy balance in the food chain in the USA (Barney, 1980).<br />

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