Abstract
Exergy efficiency is viewed as the degree of approaching reversible operation, with a value of 100 percent for a reversible process characterized by zero entropy generation or equivalently zero exergy destruction since X(destroyed) = T(0)S(gen). As such, exergy efficiency becomes a measure of thermodynamic perfection. There are different conceptual definitions of exergy efficiency, the most common ones being (1) the ratio of exergy output to exergy input η(ex) = X(output)/X(input) = 1 - (X(destroyed) + X(loss))/X(input), (2) the ratio of the product exergy to fuel exergy η(ex) = X(product)/X(fuel) = 1 - (X(destroyed) + X(loss))/X(fuel), and (3) the ratio of exergy recovered to exergy expended η(ex) = X(recovered)/X(expended) = 1 - X(destroyed)/X(expended). Most exergy efficiency definitions are formulated with steady-flow systems in mind, and they are generally applied to systems in steady operation such as power plants and refrigeration systems whose exergy content remains constant. If these definitions are to be used for closed and unsteady-flow systems, the terms need to be interpreted broadly to account for the exergy change of the systems as exergy input or output, as appropriate. In this paper, general exergy efficiency relations are developed for closed and unsteady-flow systems and their use is demonstrated with applications. Also, the practicality of the use of the term exergy loss X(loss) is questioned, and limitations on the definition η(ex) = W(act,out)/W(rev,out) are discussed.