Page 187 - Thermal Hydraulics Aspects of Liquid Metal Cooled Nuclear Reactors
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System thermal hydraulics for liquid metals                       159

           4.1.1 Turbulent Prandtl number

           In turbulent flow, the shear stress at wall surface is obtained as the sum of molecular
           and turbulent contributes:


               τ w ¼ μ ∂w      + ρε m ∂w      ¼ ρν + ε m Þ ∂w
                                       ð
                    ∂y         ∂y             ∂y
                       y¼0       y¼0            y¼0
           where ε m is the eddy diffusivity for momentum transfer (turbulent kinematic viscosity).
              Similarly, the wall heat flux is the sum of the molecular and turbulent components:


                    ∂T          ∂T               ∂T             ε m ∂T
                00
               q ¼ k                                  ¼ ρc p α +
                w         + ρc p ε q  ¼ ρc p α + ε q
                    ∂y          ∂y               ∂y             Pr t ∂y
                       y¼0         y¼0             y¼0                y¼0
           where the ε q is the eddy diffusivity for heat transfer and where the turbulent Prandtl
           number, Pr t , is defined as the ratio between heat and momentum eddy diffusivity.
              The common assumption that the turbulent Prandtl number, Pr t , is constant and is in
           the range of 0.85–1, frequently used in CFD codes, is not valid for liquid metals. In
           fact, for liquid metals, the turbulent Prandtl number seems to be more strongly
           influenced by the Reynolds and molecular Prandtl number and only slightly by the
           distance from the wall (Chen et al., 2013). Many models have been developed for
           the turbulent Prandtl number for liquid metals, starting from the one proposed by
           Aoki (1963) and the more recent correlation of Cheng and Tak (2005) for liquid metals
           and for circular tube geometry:

                1          0:45  0:2              1
                  ¼ 0:014 Re  Pr  1  exp                     ð AokiÞ
               Pr t                         0:014Re 0:45  Pr 0:2
                8
                 4:12                                Pe   1000
                >
                >
                >
                             0:01Pe
                >
                >
                >
                >                              1000 < Pe   2000    ð Cheng and TakÞ
                <
                        0:8           4     1:25
           Pr t ¼  0:018Pe    1:6+ 9   10  Pe
                >
                >
                       0:01Pe
                >
                >
                >                                   2000 < Pe   6000
                >
                >
                                 1:25
                  0:018Pe   3:4
                :       0:8
           The influence of the Peclet number on the turbulent Prandtl number can be visually
           appreciated on Fig. 4.3, where Pr t was reported as a function of the Peclet number for
           both the correlations previously mentioned.
           4.1.2 Convective heat transfer correlations
           The convective heat transfer correlations for a liquid metal flowing inside a circular
           pipe can be derived analytically using one of the correlations that gives the turbulent
           Prandtl number (see, e.g., Taler, 2016), or it can be obtained experimentally, as in the
           case of well-known Lyon (1951) and Seban and Shimazaki (1950) correlations:
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