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               Chapter 2                        Since H is a state function, we can use the integral in (2.79) to find  H for
               The First Law of Thermodynamics  any process whose initial and final states have the same pressure, whether or not
                                             the entire process occurs at constant pressure.
                                         3. Constant-volume heating with no phase change. Since V is constant, w   0.
                                             Integration of C   dq /dT and use of  U   q   w   q give
                                                                                             V
                                                          V
                                                                V
                                                                      2
                                                              ¢U       C  dT   q    V const.                (2.80)
                                                                         V      V
                                                                     1
                                             As with (2.79), Eq. (2.80) holds whether or not the heating is reversible.  H is
                                             found from  H   U   (PV)   U   V  P.
                                         4. Perfect-gas change of state. Since U and H of a perfect gas depend on T only, we
                                             integrate dU   C dT and dH   C dT [(2.68) and (2.70)] to give
                                                                          P
                                                            V
                                                              T 2                  T 2
                                                     ¢U      C 1T2  dT,   ¢H       C 1T2  dT   perf. gas    (2.81)
                                                                                    P
                                                               V
                                                            T 1                  T 1
                                             If C (T) or C (T) is known, we can use C   C   nR and integrate to find  U
                                                                                      V
                                                        P
                                                                                 P
                                                V
                                             and  H. The equations of (2.81) apply to any perfect-gas change of state includ-
                                             ing irreversible changes and changes in which P and V change. The values of
                                                                                                         2
                                             q and w depend on the path. If the process is reversible, then w     PdV
                                                                                                         1
                                                   2
                                              nR   (T/V) dV, and we can find w if we know how T varies as a function of V.
                                                   1
                                             Having found w, we use  U   q   w to find q.
                                         5. Reversible isothermal process in a perfect gas. Since U and H of the perfect gas
                                                                                                         2
                                             are functions of T only, we have  U   0 and  H   0. Also, w     PdV
                                                                                                         1
                                              nRT ln (V /V ) [Eq. (2.74)] and q   w, since q   w   U   0.
                                                         1
                                                       2
                                         6. Reversible adiabatic process in a perfect gas. The process is adiabatic, so q
                                             0. We find  U and  H from Eq. (2.81). The first law gives w   U. If C is es-
                                                                                                           V
                                                                                                         g
                                             sentially constant, the final state of the gas can be found from  P V   P V g 2
                                                                                                         1
                                                                                                              2
                                                                                                      1
                                             [Eq. (2.77)], where g   C /C .
                                                                   P
                                                                      V
                                         7. Adiabatic expansion of a perfect gas into vacuum. Here (Sec. 2.7) q   0, w
                                             0,  U   q   w   0, and  H   U   (PV)   U   nR  T   0.
                                             Equations (2.79) and (2.80) tell us how a temperature change at constant P or at
                                         constant V affects H and U. At this point, we are not yet able to find the effects of a
                                         change in P or V on H and U. This will be dealt with in Chapter 4.
                                             A word about units. Heat-capacity and latent-heat data are sometimes tabulated in
                                         calories, so q is sometimes calculated in calories. Pressures are often given in atmos-
                                                                               3
                                         pheres, so P-V work is often calculated in cm atm. The SI unit for q, w,  U, and  H
                                                                                                            3
                                         is the joule. Hence we frequently want to convert between joules, calories, and cm atm.
                                         We do this by using the values of R in (1.19) to (1.21). See Example 2.2 in Sec. 2.2.
                                             A useful strategy to find a quantity such as  U or q for a process is to write the
                                         expression for the corresponding infinitesimal quantity and then integrate this expres-
                                         sion from the initial state to the final state. For example, to find  U in an ideal-gas
                                                                                    2
                                         change of state, we write dU   C dT and  U     C (T) dT; to find q in a constant-
                                                                                    1
                                                                      V
                                                                                       V
                                                                                     2
                                         pressure process, we write dq   C dT and q     C dT. The infinitesimal change
                                                                                        P
                                                                  P
                                                                                     1
                                                                       P
                                                                                P
                                         in a state function under the condition of constant P or T or V can often be found from
                                         the appropriate partial derivative. For example, if we want dU in a constant-volume
                                         process, we use ( U/ T)   C to write  dU   C dT for  V constant, and   U
                                                                     V
                                                               V
                                                                                     V
                                          2
                                           C dT, where the integration is at constant V.
                                             V
                                          1
                                             When evaluating an integral from state 1 to 2, you can take quantities that are con-
                                         stant outside the integral, but anything that varies during the process must remain inside
                                                                                                 2
                                                                                     2
                                         the integral. Thus, for a constant-pressure process,   PdV   P   dV   P(V   V ),
                                                                                                          2
                                                                                                               1
                                                                                     1
                                                                                                 1
                                                                     2
                                                                                        2
                                         and for an isothermal process,   (nRT/V) dV   nRT   (1/V) dV   nRT ln (V /V ).
                                                                                                               1
                                                                     1
                                                                                        1
                                                                                                             2
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