A Thermodynamically Correct Treatment of Externalities with an Exergy-Based Numeraire
Abstract
:Nomenclature:
c | Molar concentration |
En | Energy, J |
e, E | Exergy, J/kg or J |
ga | Gravitational constant, m/s2 |
g,G | Gibbs free energy, J/kg; J |
h | Enthalpy, J/kg |
m | Mass flow rate, kg/s |
p | Pressure, Pa |
P | Power, W |
Q | Heat flux, W |
T | Temperature, K |
t | Time, s |
V | Velocity, m/s |
W | Work, J |
z | Elevation, m |
1. Introduction
- a) Most TE practitioners use a monetary quantifier, and therefore the environmental externality is computed in terms of some additional monetary cost to be included in the traditional production cost; but since most of the pollution is non-local, a monetary measure—no matter how detailed—ends up to be based on health and risk assessment estimates that are both fundamentally unfair and inaccurate [39]. Most recently, Tsatsaronis’ “Berlin school” [40] proposed to estimate the monetary cost of the unit exergy discharge on the basis of an analogy with the LCA indicator for the same discharge: The convenience of such an approach is though doubtful, because it introduces an additional arbitrary assumption in the TE cost allocation procedures.
- b) Since CEC (“Gliwice’s school”) and ECT (“Zaragoza’s school”), on the opposite, adopt a purely exergetic basis and completely neglect monetary costs, the need arises to introduce a functional link between the exergy of the discharges and the ensuing pollution, which can be easily proven to be impossible to find [41,42,43], because the exergy content of a stream is not related to its toxicity. Both schools resorted to including the “avoidance exergy cost” of pollution by including in the exergy flow diagrams a term representing the amount of exergy required to treat the effluents.
2. Spaceship Earth and the Environmental Externalities
- 1) An exergy inflow, Ėin, approximately equal to 225,000 TW (7.1 × 1024 J/yr = 7.1 YJ/yr) [23], consisting mainly of solar radiation (no accurate calculation is available for the cosmic radiation, which is generally assumed to amount to 0.25–0.3 of the total inflow);
- 2) An exergy outflow, Ėout approximately equal to 39,000 TW (1.23 × 1024 J/yr = 1.23 YJ/yr), consisting of low temperature back-radiation from the outer boundary of the system (a virtual sphere embedding the upper atmosphere) towards the 3 °K background;
- 3) According to the exergy flow diagram, the difference Ėd = Ėin − Ėout = 5.87 1024 J/yr is cumulatively destroyed (annihilated) by the large and small-scale processes on the planet. For comparison, the total energy use by humans on Earth (including foodstuff) amounts to approximately 0.02 YJ/yr.
- a) They continue to allocate the exergy surplus available to them (which seems to be a more proper name for Éd in this context!) in such a way to induce no major changes in the type of processes taking place in the ecosphere, in their spatial distribution and relative timescales;
- b) They react to the unavoidable fluctuations caused either by small variations of the solar input or by “internal readjustments” among some of the subsystems (evolutionary processes, local climate variations, accidental epidemics or/and extinctions, local catastrophes like droughts, floods, fires, volcanic activity, etc.) in such a way that the global amount of exergy they “destroy” (i.e., use!) remains approximately constant.
3. Exergy and Extended Exergy
3.1. The Concept of Exergy
- 1) The initial kinetic and potential energy of S are completely “recovered” into useful work. In fact, all work exchanges between S and O are entirely (and quantitatively) equivalent to exergy flows, but this property is not symmetrical, since not all energy flows can be recovered into adiabatic work. Defining a quality or exergetic factor as the ratio between the exergy and the energy content of an energy flux, all of the “high quality” forms (mechanical and electrical work, kinetic and potential energy) have an exergetic factor equal to one. Each form has its own factor: For example, thermal energy has an exergetic factor equal to its associated Carnot efficiency, reflecting the fact that, under the present stipulations, the maximum work that can be extracted from a quantity of heat Q available at a certain temperature T is equal to WQ = (1 – TO/T) Q;
- 2) If S is initially at a lower temperature than O, thermal energy will flow from O to S, with a corresponding exergy flow equal to EQ = (1 – TS/TO) Q. This amount is always positive [64];
- 4) The chemical potential of the elements in S cannot be entirely converted to work: When S comes to equilibrium with O, the most we can “recover” for the generic k-th component is the difference between the values of its Gibbs function in S and in O, each weighted by the respective concentration. In other words, we can ideally transform only a portion of the initial ΔGS into useful work, because the products of reaction must be at their respective standard environmental concentrations and chemical potentials at TO and pO;
- 5) Equation 1 can be rewritten in such a way that the different “components “of exergy are explicitly represented:
- where the suffixes indicate the usual denomination of the various terms: Physical, chemical, kinetic, potential exergy [73]. If other forms of energy fluxes are involved (magnetic, nuclear, etc.), one needs only to explicit the suffix “j” and apply the corresponding definition. Use of (3) is very convenient in the evaluation of a technological chain;
- 6) Exergy enjoys both the extensive and the additive property (E(S1 + S2) = mS1eS1 + mS2eS2);
- 7) The maximum work obtainable from the exclusive interaction of two systems Sa and Sb is |Ea – Eb|;
- 8) If a stream a undergoes a series of transformations i, j, k … z in which it receives (+) or delivers (−) the exergy rates Ei …EZ, its final exergy content is the sum of Ea+ Ei − Ej+Ek −…EZ. Thus, the net cumulative amount of exergy used in a process can be added to the pristine exergy of the input materials to obtain the global exergy embodied in the (material or immaterial) product [31,72]. This is the theoretical foundation of Szargut’s CEC and Valero’s ECT;
- 9) Neither in (2) or (3) is an implicit or explicit link detectable between exergy of a stream or substance and its toxicity.
3.2. Exergy and the Non-Energetic Production Factors
3.3. Extended Exergy Accounting
3.3.1. The Equivalent Exergy of Labor
3.3.2. The Equivalent Exergy of Capital
Country | Ėin J/yr | NW workforce | M2 €/yr | α | β | eeL MJ/work hour | eeK MJ/€ | Source |
---|---|---|---|---|---|---|---|---|
Cameroun | 2.62 1021 | 7.83 106 | 1.31 109 | 0.00014 | 1.23 | 28.67 | 612.46 | [37] |
China | 56.70 1021 | 815.00 106 | 3.52 1012 | 0.00113 | 9.28 | 49.11 | 187.16 | [60,31] |
Italy | 1.07 1021 | 24.7 106 | 2.10 1012 | 0.00746 | 2.54 | 201.40 | 13.43 | [6,37] |
Spain | 2.32 1021 | 22.2 106 | 2.22 1012 | 0.00270 | 3.17 | 176.44 | 11.76 | [61,37] |
Turkey | 3.09 1021 | 25.60 106 | 2.30 1011 | 0.00111 | 0.40 | 83.56 | 20.90 | [71,37] |
USA | 64.60 1021 | 154.00 106 | 8.18 1012 | 0.00159 | 0.33 | 415.74 | 16.64 | [83,60] |
Yemen | 3.82 1021 | 6.83 106 | 4.00 109 | 0.00008 | 10.71 | 26.96 | 863.09 | [31,33] |
Pollutant | ech (kJ/kg) | eeenv (kJ/kg) |
---|---|---|
CO | 9825 | 11800 |
NOx | 2963 | 3610 |
SO2 | 4892 | 5890 |
3.3.3. The Equivalent Exergy of the Environmental Impact
3.3.4. A Note on the Allocation Procedures of EEA
4. Two Examples of Application
4.1. Extended Exergy of the Environmental Remediation Cost for the Transportation Sector in China [48]
- 1) Under the current official accounting regulations, the M2 of China is difficult to calculate: Therefore, the GNP (gross national product) was used instead;
- 2) The yearly number of work hours in China is very low (average is about 240 work hours/yr) because the predominantly rural and scarcely industrialized population has a workload that depends on the harvesting seasons and agriculture is primitive and non-intensive. Furthermore, neither domestic work nor part-time work by minors and elderly is accounted for;
- 3) The average wage s = 280 €/yr, and is low for the same reasons as point 2 above;
- 4) The only pollutants taken under consideration in the analysis are CO, NOx and SO2, for which reliable data were available;
- 5) The effluent treatments were assumed to be post-combustion for CO (CO + O2 = CO2); catalytic reduction for NOx (2NOx = xO2 + N2) and calcination for SO2 (SO2 + CaO + 0.5O2 = CaSO4). Standard industrial processes were considered, but all reactions are assumed to be complete.
- 6) Material costs were taken from the Chinese market 2008.
Transportation mode | Labor exergy, EEL (J/yr) | EEL/Ėin(a) | Capital exergy, EEK (J/yr) | EEK/Ėin | Environmental Remediation exergy, EEO (J/yr) | EEO/Ėin |
---|---|---|---|---|---|---|
Highways | 6.72 × 1018 | 7.65% | 8.06 × 1018 | 9.17% | 2.22 × 1018 | 2.53% |
Railways | 4.71 × 1018 | 5.36% | 2.38 × 1018 | 2.71% | 3.21 × 1015 | 0.004% |
Waterways | 1.18 × 1018 | 1.34% | 1.17 × 1018 | 1.34% | 1.31 × 1016 | 0.015% |
Civil aviation | 6.87 × 1017 | 0.78% | 1.72 × 1019 | 19.58% | 1.88 × 1015 | 0.002% |
Total | 1.33 × 1019 | 15.14% | 1.72 × 1019 | 19.60% | 2.24 × 1018 | 2.5% |
4.2. Extended Exergy of the Environmental Remediation Cost for the Transportation Sector in Turkey [59]
- 1) The only pollutants taken under consideration in the analysis are CO2, N2O and CH4: all other emissions were converted into their accepted CO2 equivalents (Table 4);
- 2) The effluent treatments were assumed to be post-combustion for CH4 (CH4 + 2O2 = CO2 + 2H2O); catalytic reduction for N2O (2N2O = O2 + 2N2) and calcination for CO2 (CO2 + CaO = CaCO3). Standard industrial processes were considered, but all reactions are assumed to be complete.
- 3) Material costs were taken from the Turkish market 2006.
Pollutant | eeO (kJ/kg) | EEO (J/yr) |
---|---|---|
CO2 | 57,600 | 2.52 × 1018 |
N2O | 10,600 | 0.47 × 1015 |
CH4 | 322,400 | 0.55 × 1015 |
Total | 25.22 × 1018 |
Labor exergyEEL (J/yr) | EEL/Ėin(a) | Capital ExergyEEK (J/yr) | EEK/Ėin | Environmental Remediation ExergyEEO (J/yr) | EEO/Ėin |
---|---|---|---|---|---|
0.41 × 1018 | 2% | 3.85 × 1018 | 20% | 2.61 × 1018 | 13% |
5. Conclusions
Conflict of Interest
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Sciubba, E. A Thermodynamically Correct Treatment of Externalities with an Exergy-Based Numeraire. Sustainability 2012, 4, 933-957. https://doi.org/10.3390/su4050933
Sciubba E. A Thermodynamically Correct Treatment of Externalities with an Exergy-Based Numeraire. Sustainability. 2012; 4(5):933-957. https://doi.org/10.3390/su4050933
Chicago/Turabian StyleSciubba, Enrico. 2012. "A Thermodynamically Correct Treatment of Externalities with an Exergy-Based Numeraire" Sustainability 4, no. 5: 933-957. https://doi.org/10.3390/su4050933
APA StyleSciubba, E. (2012). A Thermodynamically Correct Treatment of Externalities with an Exergy-Based Numeraire. Sustainability, 4(5), 933-957. https://doi.org/10.3390/su4050933