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Heat and mass transfers in the context of energy geostructures  87


                      The motion of fluids, which involves a movement of the particles bringing
                   their thermal energy in proximity to each other, is the result of a force. When the
                   force that causes the motion of the fluid is due entirely to density variations
                   caused by a nonuniform temperature distribution, that is a temperature gradient,
                   the convection phenomenon is called free or natural convection. When the force
                   that causes the motion of the fluid is due to any other cause, the convection phe-
                   nomenon is termed forced convection. Free convection is an example of the coupling
                   between heat and mass transfers.
                      In the analysis of motion of fluids, it is relevant to distinguish problems of internal
                   flow, external flow and seepage flow. In internal flow problems, the fluid in motion is
                   completely bounded by a surface (e.g. a heat carrier fluid circulating in a pipe or air
                   flowing in an underground built environment). In external flow problems, the fluid in
                   motion is not completely bounded by a surface (e.g. surface air flowing over the
                   ground). In seepage flow problems, the fluid is in motion across a permeable material
                   medium (e.g. groundwater flowing within soils).
                      The physical phenomenon of convection heat transfer can be explained, for exam-
                   ple with reference to a fluid in motion relative to a bounding surface at a different
                   temperature, which at a meaningful scale can be considered as a plane wall. This prob-
                   lem is represented in Fig. 3.7 considering a convection phenomenon that can charac-
                   terise, for example an energy tunnel. The temperature varies from a value T s at the
                   surface (e.g. y 5 0) to a temperature T N , T s in the fluid bulk. In this case, heat trans-
                   fer occurs from the wall to the bulk of the fluid. The opposite is true for T s , T N .At
                   the surface wall, convection heat transfer occurs because of the sole molecular diffu-
                   sion mechanism, as the velocity of the fluid is equal to zero. Beyond the surface and
                   until T s 6¼ T N , the mechanism of bulk motion contributes to the overall convection
                   heat transfer phenomenon.





















                   Figure 3.7 Heat transfer by convection at the surface of an energy tunnel.
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