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24                               Entropy Analysis in Thermal Engineering Systems


          Clausius, who uses it fundamentally in his mathematical investigations” [23].
          Indeed, Rudolf Clausius derived an equation in 1850 similar to that given
          by Eq. (2.13) in the following form [24]:


                                           ð
                                     C ¼ Aa + tÞ                      (2.14)
          where C denotes the inverse of Carnot’s function, A designates the equiv-
          alent of heat for the unit of work, i.e., inverse of J in Eq. (2.13), and a¼273 is
          the inverse of the expansion coefficient of air, i.e., 0.003665 determined
          from the experiments of Magnus and Regnault. The relation between
          the absolute temperature scale and centigrade, [K]¼[°C]+a, was given
          by William Rankine in a paper read on February 4, 1850 before the Royale
          Society of Edinburgh [25]. Clausius also arrived at the same relation [26]
          with a difference that in the Clausius relation a¼273, whereas in that of
          Rankine a¼274.6.
             Rankine, in a subsequent paper, presented an analytical formulation to
          derive an expression for the efficiency of the Carnot cycle [27].


                                         T 1  T 0
                                    W
                                       ¼                              (2.15)
                                    Q 1     T 1
          where Q 1 is the total heat supplied, T 1 and T 0 denote the temperature at
          which heat is supplied to and rejected by the working substance,
          respectively.
             A remarkable conclusion enunciated by Rankine is that “Carnot’s Law is
          not an independent principle in the theory of heat; but is deducible, as a consequence,
          from the equations of the mutual conversion of heat and expansive power.” An equa-
          tion analogous to Eq. (2.15) was also obtained by Thomson using the com-
          bined gas laws; i.e., Eq. (2.12), and Poisson’s equations, which was published
          as a note to a paper authored by Joule on air engines [28].
             After presenting a modified definition for the absolute temperature scale,
          Thomson presented mathematical expressions of the first and second laws of
          thermodynamics for a system undergoing a reversible process [21].

                               ð       0        n 1 + H t Þ ¼ 0       (2.16)
                                                      n
                          W + JH t + H t + … + H t
                                    0        n 1    n
                               +  H t  + … +  H t  +  H t  ¼ 0        (2.17)
                             H t
                                   0        n 1    n
                             t    t        t       t
                                             0,
          where W denotes the work done, H t , H t …, H t n 1, H t n designate the quan-
                                              0    n 1 , t , respectively.
                                                        n
          tities of heat taken in at temperatures t, t , …, t
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