Page 321 - Mechanical Engineers' Handbook (Volume 4)
P. 321

310   Heat Exchangers, Vaporizers, Condensers




















                                              Figure 15 Condensation profiles illustrated.


                          Heat-Transfer Coefficients, Pure Components
                          For condensers, it is particularly important to be able to estimate the two-phase flow regime
                          in order to predict the heat-transfer coefficient accurately. This is because completely dif-
                          ferent types of correlations are required for the two major flow regimes.


                          Shear-Controlled Flow. The vapor shear force on the condensate is much greater than the
                          gravity force. This condition can be expected, according to Ref. 18, when
                                                          J   1.5                             (27)
                                                           g
                          where
                                                    J        (Gy) 2    0.5

                                                     g                                        (28)
                                                         gD   (      )
                                                            j
                                                               l
                                                             v
                                                                   v
                          For shear-controlled flow, the condensate film heat-transfer coefficient (h ) is a function of
                                                                                   cƒ
                          the convective heat-transfer coefficient for liquid flowing alone and the two-phase pressure
                             18
                          drop :
                                                       h cƒ    h (  )                         (29)
                                                               20.45
                                                             l
                                                               l
                                                        h   h (1   y) 0.8                     (30)
                                                         l
                                                             i
                          or
                                          h   h (1   y) 0.6                                   (31)
                                               o
                                           l
                                                  C    1
                                             1                                                (32)
                                          2
                                          l
                                                 X    X  2
                                                   tt  tt
                                          C   20 (tubeside flow),
                                         X                      C   9 (shellside flow)
                                                                 0.1
                                                           0.5
                                                     0.9


                                               1   y
                                                         v
                                                                l
                                          tt
                                                 y        t     v                             (33)
                                             liquid viscosity,      vapor viscosity
                                           l
                                                               v
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