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36       BASICS  OF  FLUID  MECHANICS  AND  INTRODUCTION  TO  CFD




                                               de  =  Tds  —  pd  (*)  ;
                                                                     p

                 This  last  differential  relation  could  be  the  departure  point  in  the  ther-
              modynamical  study  of  the  ideal  fluids.  If  the  internal  energy  e  is  given

              as  a  function  of  the  independent  parameters  s  and  ;  =  v,  Le.,  if  we
             know  e  =  €(s,v),  then  we  will  immediately  have  the  equations  of  state
             p=  —  9  (s,v)  and  T  =  ae  (s,v)  or,  in  other  words,  the  function  é(s,  v)  ,
             determining  the  thermodynamical  state  of  the  fluid,  is  a  thermodynami-

              cal  potential  for  this  fluid.  Obviously,  this  does  not  occur  if e  is  given  as  a
             function  of  other  parameters  when  we  should  consider  other  appropriate
             thermodynamical  potentials.
                 If  the  inviscid  fluid  is  incompressible,  from  d  (4)  =  dy  =  0  we  have

             that  T  =  T'(s)  or  s  =  8(T)  and  hence  e  =  €(T).  More,  if  in  the  energy

             equation,  written  under  the  form


                                           pé  =  [T]  -(D]  —  divg  +  pra,


             we  accept  the  use  of  the  Fourier  law  q  =  —  xgradT,  where  x  is  the
             thermal  conduction  coefficient  which  is  supposed  to  be  positive  (which

             expresses  that  the  heat  flux  is  opposite  to  the  temperature  gradient),  we
             get  finally



                                            pe  =  div  (ygradT)  +  pra.

                As  e  =  €(T)  and  rg  (the  radiation  heat)  is  given  together                  with

              the  external  mass  forces,  the  above  equation  with  appropriate  initial
              and  boundary  conditions,  allows  us  to  determine  the  temperature  T
              separately  from  the  fluid  flow  which  could  be  made  precise  by  considering
             only  the  Euler  equations  and  the  equation  of  continuity.
                 This  dissociation  will  not  be  possible,  in  general,  within  the  compress-
             ible  case.  Even  the  simplest  statics  (equilibrium)  problems  for  the  fluids
             testify  that.

                 An  important  situation  for  the  compressible  fluids  is  that  of  the  perfect
             fluids  (gases),  the  air  being  one  of  them.
                 By  aperfect  gas,  we  understand  an  ideal  gas  which  is  characterized  by
             the  equation  of  state  (Clapeyron)  p  =  pRT  (where  R  is  a  characteristic

             constant).  For  such  a  perfect  gas  the  relation  Cp,  —  Cy  =  T  (2).  (3t),
             becomes  Cy  —  Cy,  =  R,even  if  C,  and  C,  are  functions  of  temperature
              (Joule).  Since  (6g),  =  CpdT,  (6q),,  =  CydT,  the  first  law  of  thermody-

             namics  under  the  form  dq  =  de  +  pdv,  leads  to
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