Abstract
The physical exergy of all internal and external streams is determined from the thermodynamic properties such as enthalpy, the entropy of the working fluid at each state points and temperature of dead state. The chemical exergy is estimated based on the concentration of individual species in the mixture with respect to the reference fluid then the total exergy is determined by summing up the physical exergy and the chemical exergy. The important objective of this paper is the thermoeconomic comparisons of the vapour adsorption refrigeration system working under activated carbon (AC)–R134a and AC–diethyl ether pairs. A thermodynamic analysis is the preliminary work of the thermoeconomic comparisons.
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