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2. Overall Heat Transfer



                  A overall heat-transfer is named the process of  thermal energy flow from one fluid
            to other through the one layer or multi-layered wall of free-form. The heat-transfer is a


            complicate process of heat transference. It includes a heat conduction, convection and
            radiation. The typical examples of a overall heat-transfer is a  heat flow from hot water


            to room  air through the walls of heater batteries of the central heating, transmission of

            heat from  room  air to outside air through the walls.

                  A overall heat-transfer from inside air to outside air there is a complex process:

               - inside                                 → convection;

               - in the wall construction     → conduction ;

               - outside                               → also convection;



                  The heat energy flow with overall heat transfer coefficient:



                                        4
                          I
                          Q   k  dF (T   T 2 4 )      (W)                                                                 (2.1)
                                       1
                                                                       2
                    k -  the overall heat transfer coefficient W/(m •K)
                                                  2
                   dF  – surface of the wall, m

                   T 1   – temperature of the inside fluid, K or °C

                    T 2  -  temperature of the outside fluid, K or °C

                 The overall  heat  transfer  coefficient ,  in thermodynamics and  in mechanics, is  the

             proportionality coefficient between the heat flow and the thermodynamic driving force

            ΔT for the heat flow


                                                   q     W
                                                               k      ,                                                                 (2.2)
                                                   T   m 2 K

                                             2
            where:     q -  heat flow, W/m ;
                           ΔT - difference in temperature between the solid surface and surrounding fluid

            area, K.






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