Page 143 - Industrial Ventilation Design Guidebook
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4 i HF:AT AND MASS TRANSFER                                               105
















                       FIGURE 4.24  Laminar and turbulent boundary layers and temperature distribution inside the
                       boundary layer.


                           3. In a turbulent boundary layer, flow takes place in the direction
                             perpendicular to the surface over which the flow occurs.
                           A heat transfer factor (a) between the fluid and surface is defined as



                       where 0 is the temperature difference between the surface and the fluid at a
                       long distance from the surface.
                           When heat transfer occurs by conduction through the boundary layer,




                       where 8 is the thickness of the boundary layer, and the unit of a is W m " K .
                       The heat transfer factor a thus decreases as the boundary layer thickness in-
                       creases. The following discussion gives some indication of the range of the
                       heat transfer values obtained due to the different modes of convective heat
                       transfer.
                           Next we give some values of a to give an idea of the magnitude of the heat
                       transfer:

                                                                    2
                                                             a, W m-  K- 1
                                          Free convection      3.5-50
                                           Forced convection, air  10-500
                                           Forced convection, liquid  100-5000


                       A liquid has a higher rate of conductivity than a gas.
                           In boiling convection, liquid motion is created by steam bubbles breaking
                       loose from the surface.
                           If steam condenses on a surface, there is no boundary layer; the resis-
                       tance to heat flow is due to scale, metal thickness, and the condensed liq-
                       uid layer, resulting in a high heat transfer factor. A thin layer of air or
                       other noncondensing gas forms at the surface through which the steam dif-
                       fuses. The heat transfer factor diminishes rapidly but is considerably
                       higher than in dry convection.
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