Page 118 - Mechanical Engineers' Handbook (Volume 4)
P. 118

6 Relations among Thermodynamic Properties  107

                                                                 Tv  2
                                                         c   c    K
                                                         P
                                                              v
                                                      
               v
                                                          1
                                                               	v
                                                          c P  T  	T  P
                           The general equations relating the derived properties (u, h, s) to measurable quantities are
                                                  du   cdT   T
                                                                 	P
                                                                       Pdv
                                                       v
                                                                 	T
                                                dh   cdT
                                                                    v
                                                                  	v
                                                               T
                                                                         v dP
                                                      P
                                                                  	T
                                                      	v
                                                                              	v
                                             c  dT                   P c  dT
                                         ds    v          dv or ds     P          dP
                                              T       	T              T       	T
                                                         v                       P
                           These relations also suggest the following identities:
                                                  T       c
                                                     	s
                                                                 	h
                                                                           	s
                                            	u
                                            	T  v    	T    v     	T  P    T  	T  P    c P
                           The relationships between thermodynamic properties and the analyses associated with ap-
                           plying the laws of thermodynamics are simplified considerably in cases where the pure
                           substance exhibits ideal gas behavior. As shown in Fig. 3, this behavior sets in at sufficiently
                           high temperatures and low pressures; in this limit, the (P, v, T) surface is fitted closely by
                           the simple expression
                                                        Pv
                                                            R (constant)
                                                        T
                           where R is the ideal gas constant of the substance of interest (Table 1). The formulas for
                           internal energy, enthalpy, and entropy, which concluded the preceding section, assume the
                           following form in the ideal-gas limit:
                                                    du   cdT     c   c (T)
                                                          v
                                                                  v
                                                                      v
                                                dh   cdT     c   c (T)   c   R
                                                                  P
                                                              P
                                                                         v
                                                      P
                                       c      R            c      R             c      c
                                  ds    v  dT    dv or ds    P  dT    dP or ds    v  dP    P  dv
                                       T      v             T     P             P      v
                           If the coefficients c and c are constant in the temperature domain of interest, then the
                                           v
                                                 P
                           changes in specific internal energy, enthalpy, and entropy relative to a reference state ( )
                                                                                                  0
                           are given by the formulas
                                                      u   u   c (T   T )
                                                           0   v      0
                                           h   h   c (T   T )   (where h   u   RT )
                                                    P
                                                                                 0
                                                                           0
                                                                       0
                                                           0
                                                0
                                                                T       v
                                                    s   s   c ln    R ln
                                                        0
                                                            v
                                                                T 0     v 0
                                                                T       P
                                                    s   s   c ln    R ln
                                                            P
                                                        0
                                                                T 0     P 0
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