Page 139 - Mechanical Engineer's Data Handbook
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128                                                 MECHANICAL  ENGINEER'S DATA  HANDBOOK

             Refrigeration effect RE = cp( TI - T3) + cpq,( T3 - T,)

             Work in  W=cp--  (T2 -   cpqt( T3 - T,)
                            VC
                                        RE
             Coefficient of  performance COP = -
                                        W
                      T,  ( )~
                   T
             where: A=        (   I, qt = turbine isentropic effi-   4    I      I
                      -=
                      m
                   m
                   12  13  \Pl/
             ciency, qc =compressor  isentropic efficiency.

             3.14   Heat transfer

             Heat may be transmitted by conduction, convection or
             radiation.


             3.14.  I  Conduction

             Heat transfer by conduction is the transfer of heat from
             one part of a substance to another without appreciable
             displacement of  the molecules of  the  substance, e.g.
             heat flow along a bar heated at one end. This section
             deals with conduction  of  heat  through a flat wall, a
             composite wall,  a  cylindrical wall  and  a  composite
             cylindrical wall. A table of thermal-conductivity coeffi-
             cients is given.
                                                                            x
                                                                                1
                                                         Thermal resistance R = - -
                                                                              =
                                                                           kA  UA
             3.14.2   Conduction through wall
                                                         Conduction from JIuid to Jluid through wall
             Let:
              k=conductivity  of  wall, Wm-lK-'          In  this  case  the  surface coefficients are  taken  into
              A=area  of  wall, m2                       account.
              x = thickness of  wall, m                               kA
              t = temperature ("C)                       q=Aha(ta-tl)=-(tl   -t2)=  Ahb(t2-tb)
             q = heat flow rate, W                                    X
             h=heat  transfer coefficient, WrnW2K-'
             U =overall  heat transfer coefficient, Wm-2K-1
             R = thermal resistance KW-
                        kA
             Heat flow q=-(t,-t,)
                         X
                                         k
             Overall heat transfer coefficient  U =-
                                         X
             Therefore, q=  UA(t, -t2)
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