Page 355 - Mechanical Engineers' Handbook (Volume 4)
P. 355

344   Heat Pipes

           3.5 Sonic Limit
                          When the vapor velocity at the exit of the evaporating section reaches the local sound speed,
                          the vapor flow is choked. As the chocked flow occurs, the vapor flow rate will not respond
                          with the amount of heat added in the evaporator. The heat pipe has reached the maximum
                          heat transport, which is called the sonic limit. If the vapor flow in the heat pipe can be
                          approximated as one-dimensional flow with the assumptions of negligible frictional force
                          and ideal gas, the sonic limit can be readily derived from the conservation of energy and
                          momentum equations as follows:
                                                  q   A   h      RT     1/2
                                                                v
                                                                  v 0
                                                   s
                                                           ƒg
                                                        vv
                                                              2(    1)                        (26)
                                                                 v
                          where T is the stagnation temperature, A and   are the cross-sectional area and vapor
                                                           v
                                                                  v
                                0
                          density, respectively, at the location where the local sound speed is reached. It should be
                          noted that this might occur at the exit to the evaporator or any location in the condenser
                          section if the cross-sectional area of vapor flow path changes.
           3.6  Effective Thermal Conductivity
                          While those operating limitations described above dominate the design of a heat pipe, the
                          effective thermal conductivity provided by a heat pipe is a key factor for designing a highly
                          efficient heat-pipe cooling device. The effective thermal conductivity, k , is related to the
                                                                                  eff
                          total temperature drop,  T total ,as
                                                              qL
                                                        k eff     eff                         (27)
                                                             A  T total
                                                              h
                          where A is the total cross-sectional area of heat pipe. The total temperature drop,  T  total ,
                                h
                          across the heat pipe is the sum of the temperature drop across the evaporator shell,  T e,shell ;
                          the temperature drop across the wick structure in the evaporator,  T e,wick ; the temperature
                          drop through the evaporating thin film,  T e,film ; the temperature drop in the vapor flow,  T ;
                                                                                                v
                          the temperature drop across the condensate film,  T c,film ; the temperature drop across the
                          wick structure at the condenser,  T c,wick ; and the temperature drop across the condenser shell,
                           T c,shell , i.e.,
                                 t total     T e,shell     T e,wick     T e,film     T    T c,film     T c,wick     T c,shell  (28)
                                                                  v
                          Temperature Drops across Shell and Wick
                          The temperature drop through the case shell material at both the evaporator and the condenser
                          can be calculated by
                                                               q
                                                        T e,shell     ee,shell                (29)
                                                                k shell
                          and
                                                               q
                                                        T c,shell     cc,shell                (30)
                                                                k shell
                          respectively. After heat is traveled through the wall, the heat reaches the working fluid in
                          the wick. Provided that the wick is saturated with the working fluid and no boiling occurs
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