Thermodynamic Analysis of a Vapor Absorption System Using Modified Gouy-Stodola Equation

In this paper, the exergy analysis of vapor absorption
refrigeration system using LiBr-H2O as working fluid is carried out
with the modified Gouy-Stodola approach rather than the classical
Gouy-Stodola equation and effect of varying input parameters is also
studied on the performance of the system. As the modified approach
uses the concept of effective temperature, the mathematical
expressions for effective temperature have been formulated and
calculated for each component of the system. Various constraints and
equations are used to develop program in EES to solve these
equations. The main aim of this analysis is to determine the
performance of the system and the components having major
irreversible loss. Results show that exergy destruction rate is
considerable in absorber and generator followed by evaporator and
condenser. There is an increase in exergy destruction in generator,
absorber and condenser and decrease in the evaporator by the
modified approach as compared to the conventional approach. The
value of exergy determined by the modified Gouy-Stodola equation
deviates maximum i.e. 26% in the generator as compared to the
exergy calculated by the classical Gouy-Stodola method.





References:
[1] M.A. Hammad, M.S.Audi, Performance of a Solar LiBr-Water
Absorption Refrigeration System, Renewable Energy, Vol. 2, 1992, pp.
275-282.
[2] S.M. Deng, W.B. Ma, Experimental studies on the characteristics of an
absorber using LiBr/H2O solution as working fluid, International
Journal of Refrigeration, Vol. 22, 1999, pp. 293–301.
[3] Omer Kaynakli, Muhsin Kilic, Theoretical study on the effect of
operating conditions on performance of absorption refrigeration system,
Energy Conversion and Management, Vol. 48, 2007, pp. 599–607.
[4] R.D. Misra, P.K. Sahoob, A. Gupta, Thermoeconomic evaluation and
optimization of a double effect H2O/LiBr vapor-absorption refrigeration
system, International Journal of Refrigeration, Vol. 28, 2005, pp. 331–
343.
[5] S.C. Kaushik, Akhilesh Arora, Energy and exergy analysis of single
effect and series flow double effect water–lithium bromide absorption
refrigeration systems, International Journal of Refrigeration, Vol. 32,
2009, pp. 1247–1258.
[6] Tatiana Morosuk, George Tsatsaronis, A new approach to the exergy
analysis of absorption refrigeration machines, Energy, Vol. 33, 2008, pp.
890–907.
[7] I. Horuz, T.M.S. Callander, Experimental investigation of vapor
absorption refrigeration system, International Journal of Refrigeration,
Vol. 27, 2004, pp. 10–16.
[8] M.Izquierdo, J.D.Marcos, M.E.Palacios, A.Gonzalez Gil, Experimental
evaluation of a low-power direct air-cooled double-effect LiBr-H2O
absorption prototype, Energy, Vol. 37, 2012, pp. 737–748.
[9] Lampinen, M.J. Wiksten R, Theory of effective heat absorbing and heat
emitting temperatures in entropy and exergy analysis with applications
to flow systems and combustion process, Journal of Non-equilibrium
Thermodynamics, Vol. 31, 2006, pp. 257-291.
[10] Holmberg, H., Ruohonen, P. and Ahtila, P, Determination of the real
loss of power for a condensing and a backpressure turbine by means of
second law analysis, Entropy, Vol. 11, 2009, pp. 702-712.
[11] Patek J, Klomfar J, A computationally effective formulation of the
Thermodynamic properties of LiBr–H2O solutions from 273 to 500 K
over full composition range, International Journal of Refrigeration, Vol.
29, 2006, pp. 566–578.