While exergy analysis is by now commonly used on the system level to identify losses and recommend ways for reducing them, its use on the “intrinsic”, field, level where the exergy of a process is calculated as a function of location and time, is still developing. Intrinsic exergy analysis is a most useful method for identifying and understanding the specific reasons for exergy losses in a process, and in devising methods for their reduction. A good example, which is the sample case of this paper, is the analysis of exergy losses in combustion processes, which are known to be responsible for around 30 % of the fuel potential to produce power. In this paper we develop a methodology for intrinsic exergy analysis and for its use for process improvement, using the case of combustion of a n-heptane droplet as example. The time-dependent continuity, energy and species conservation equations together with the reaction kinetics, state equations, and temperature and concentration dependent transport properties, are solved numerically to determine the temperature and concentrations fields. These results are then used to calculate the rates of local entropy generation to determine the spatial and temporal irreversibilities produced during the combustion process, as well as the exergy efficiency. The results obtained indicate, among other things, that after ignition has taken place, the exergy loss (or entropy generation) component most responsible for the overall exergy loss is the chemical entropy, having the same order of magnitude as the rest of the entropy generation terms combined for all the cases evaluated. The computed exergy efficiency for the base case is 68.4%, in agreement with previous droplet combustion exergy studies. To develop guidelines for the process improvement, the sensitivity of the second law efficiency to the initial gas temperature (Tgi), reaction rate (ω), and combustion duration were analyzed. The results generated several promising improvement avenues.

1.
Dunbar
WR
,
Lior
N
,
Gaggioli
RA.
The component equations of energy and exergy
.
ASME J Energy Resour Technol
,
1992
;
114
:
75
83
.
2.
Moran, M.J., Availability analysis—a guide to efficient energy use (corrected edition). New York: ASME, 1989.
3.
Gouy
G.
,
About available energy (in French)
,
J. Physique II
,
8
(
1889
)
501
518
.
4.
Stodola
A.
The cyclic process of the gas engine.
(in German)
Z. VDI
1898
;
32
(
38
):
1086
91
5.
Gibbs JW. Collected Works, 1. New Haven: Yale University Press; 1948.
6.
Keenan
J. H.
,
A steam chart for second law analysis
,
Mech. Eng.
54
(
3
) (
1932
)
195
204
.
7.
J.H. Keenan, J. H., Thermodynamics, 1941, Wiley, N. Y.
8.
Bosˇnjakovic’
F.
Fight against irreversibilities.
(in German)
Arch Warmewirt
1938
;
19
(
1
):
1
2
9.
Rant
Z.
Exergy, a new word for technical available work.
(in German)
Forsch Ing Wes
1956
;
22
(
1
):
36
7
.
10.
Denbigh
K. G.
,
The second-law efficiency of chemical processes
,
Chem. Eng. Sci.
,
6
(
1
) (
1956
)
1
9
.
1.
Leites
I. L.
,
Sama
D. A.
,
Lior
N.
, “
The theory and practice of energy saving in the chemical industry: some methods for reducing thermodynamic irreversibility in chemical technology processes
,”
Energy
,
28
, 1,
2003
, pp.
55
97
;
2.
Corrigendum
,
Energy
,
29
,
2
,
2004
,
301
304
.
1.
Szargut J, Morris DR, Steward FR. Exergy analysis of thermal, chemical and metallurgical processes. New York: Hemisphere; 1988
2.
Bejan A. Entropy generation minimization: the method of thermodynamic optimization of finite-size systems and finitetime processes. Boca Raton, FL: CRC Press; 1996.
3.
Bejan. Advanced engineering thermodynamics. 2nd ed. New York: Wiley; 1997.
4.
Moran MJ, Shapiro NH. Fundamentals of engineering thermodynamics. 5th ed. Hoboken, NJ: Wiley; 2004.
5.
Bejan, A., Tstsaronis, G., Moran, M. Thermal design and optimization. New York: John Wiley and Sons, Inc., 1996.
6.
Noam Lior and Na Zhang, “Energy, exergy, and Second Law performance criteria,” Proc. ECOS 2005, 1, pp. 437–445, June 20–22, 2005, Trondheim, Norway.
7.
Dunbar
W. R.
,
Lior
N.
,
Gaggioli
R. A.
,
The component equations of energy and exergy
,
ASME J. Energy Resources Technology
,
114
, (
1992
)
75
83
.
8.
Krickwood
J. G.
and
Crawford
B.
(
1952
).
The macroscopic equation of transport
.
J. Phys. Chem.
56
,
1048
1048
.
9.
J.O. Hirschfelder, C.F. Curtiss, R.B. Bird, R. B. 1954, Molecular Theory of Gases and Liquids. 1954, Wiley, New York.
1.
Leites
I. L.
,
Sama
D. A.
,
Lior
N.
,
The theory and practice of energy saving in the chemical industry: some methods for reducing thermodynamic irreversibility in chemical technology processes
.
Energy
2003
;
28
(
1
):
55
97
;
2.
Corrigendum
,
Energy
2004
;
29
(
2
)
301
304
.
1.
Gaggioli, R. A., Yoon, J. J., Patulski, S. A., Latus, A. J., and Obert, E. F. (1975). Pinpointing the real inefficiencies in power plants and energy systems. In Gaggioli, R. A. (Ed.). Proc. Amer. Power Conf. Washington, D.C. pp. 671–679.
2.
Dunbar
W. R.
,
Lior
N.
,
Gaggioli
R. A.
,
Combining fuel cells with fuel-fired power plants for improved exergy efficiency
,”
Energy
,
16
(
1991
)
1259
1274
.
3.
Dunbar
W. R.
,
Lior
N.
,
Sources of combustion irreversibility
,”
Combustion Sci. and Tech.
,
103
(
1994
)
41
61
.
4.
Arpaci
V.
,
Selamet
A.
1988
,
Entropy production in flames
.
Combust. Flame
1988;
73
:
251
259
.
5.
Stanciu
D.
,
Isvoranu
D.
,
Marinescu
M.
,
Gogus
Y.
Second law analysis of diffusion flames
.
Int. J. Appl. Thermodynamics
2001
;
4
(
1
):
1
18
.
6.
Puri
I. K.
Second law analysis of convective droplet burning
.
Int. J. Heat Mass Transfer
1992
;
35
:
2571
2578
.
7.
Beretta
G. P.
,
Keck
J. C.
Energy and entropy balances in a combustion chamber: analytical solution
.
Comb. Sci. Technol.
1983
;
30
:
19
29
.
8.
Teng
H.
,
Kinoshita
C. M.
,
Masutani
S. M.
,
Zhou
J.
Entropy generation in multicomponent reacting flows
.
ASME J. Energy Resources Technol.
1998
;
120
:
226
232
.
9.
W.R. Dunbar, N. Lior, A Breakdown of the exergy losses in combustion, Proc. World Energy Conf., Florence, Italy, Pergamon Press, Oxford (1990) 347–358.
10.
Caton
J. A.
On the destruction of availability (exergy) due to combustion processes - with specific application to internal-combustion engines
.
Energy
2000
;
25
:
1097
1117
.
11.
Hiwase
S. D.
,
Datta
A.
,
Som
S. K.
,
1998
,
Entropy balance and exergy analysis of the process of droplet combustion
,
J. Phys. D: Appl. Phys.
,
31
(
13
) (1998)
1601
1610
.
12.
Datta
A.
;
Som
S. K.
,
1999
, “
Thermodynamic irreversibilities and second law analysis in a spray combustion process
,”
Comb. Sci. Technol.
,
142
, pp.
29
54
.
13.
N. Lior, W. Sarmiento-Darkin, H. S. Al-Sharqawi, “The Exergy Fields in Transport Processes: Their Calculation and Use,” accepted for publication in ENERGY - The International Journal.
14.
W. Sarmiento-Darkin, N. Lior. “Modeling and Exergy analysis of a burning fuel droplet,” MSB Thesis Mechanical Engineering and Applied Sciences of the University of Pennsylvania, PA, 2004.
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