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2.10 HELMHOLTZ ENERGY (HELMHOLTZ FUNCTION)              23




                  In the previous section the criteria for equilibrium were discussed and these were derived in terms
               of DS) E . The variation of entropy is not always easy to visualise, and it would be more useful if the
               criteria could be derived in a more tangible form related to other properties of the system under
               consideration. Consider the arrangements in Fig. 2.4(a) and (b). Figure 2.4(a) shows a system A, which
               is a general system of constant composition in which the work output, dW, can be either shaft or
               displacement work, or a combination of both. Figure 2.4(b) is a more specific example in which the
               work output is displacement work, pdV; the system in Fig. 2.4(b) is easier to understand.
                  In both arrangements, system A is a closed system (i.e. there are no mass transfers) which delivers
               an infinitesimal quantity of heat, dQ, in a reversible manner to the heat engine E R . The heat engine then
               rejects a quantity of heat dQ 0 to a reservoir, e.g. the atmosphere, at temperature T 0 .
                  Let dE,dVand dS denote the changes in internal energy, volume and entropy of the system, which
               is of constant, invariant composition. For a specified change of state these quantities, which are
               changes in properties, would be independent of the process or work done. Applying the First Law of
               Thermodynamics (Eqn (1.7)) to system A gives

                                                 dW ¼ dE þ dQ                               (2.21)
                  If the heat engine (E R ) and system A are considered to constitute another system, system B. Then,
               applying the First Law of Thermodynamics to system B gives

                                          dW net ¼ dW þ dW R ¼ dE þ dQ 0                    (2.22)
               where dW þ dW R ¼ net work done by the heat engine and system A. Since the heat engine is internally
               reversible, and the entropy flow on either side is equal, then

                                                    dQ 0  dQ
                                                        ¼                                   (2.23)
                                                    T 0   T


                        (a)                              (b)
                                           System B
                                                                            System B
                               System A                         System A
                                                    δW                                δW
                                                               p
                                  T                                       p
                                                                           0

                                   δQ                              δQ
                                                                                δW R
                                                 δW R
                                 E R                             E R

                                   δQ 0
                                                                   δQ 0
                              Reservoir T                     Reservoir
                                       0                              T 0
               FIGURE 2.4
               Maximum work achievable from a system.
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