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§9.2  Temperature and Pressure Dependence of Thermal Conductivity  273

                           for  rough  estimates  for  polyatomic  materials.  It should  not be used  in the neighborhood
                           of  the critical point.  1
                              It  can be  seen  that the thermal conductivity  of  a gas  approaches  a limiting  function
                           of  T at  low  pressures;  for  most  gases  this  limit  is  reached  at  about  1 atm  pressure.  The
                           thermal  conductivities  of  gases  at  low  density  increase with  increasing  temperature,
                           whereas  the thermal conductivities  of  most  liquids decrease with  increasing temperature.
                           The  correlation  is  less  reliable  in  the liquid  region;  polar  or  associated  liquids,  such  as
                           water,  may  exhibit  a  maximum  in  the  curve  of  к  versus  T.  The  main  virtue  of  the
                           corresponding-states  chart  is  that one gets  a  global  view  of  the behavior  of  the thermal
                           conductivity  of gases and  liquids.
                              The  quantity k  may be estimated  in one of two ways:  (i) given  A: at a known  temper-
                                           c
                           ature and  pressure,  preferably  close  to the conditions at which  к is  to be  estimated, one
                           can  read  k  from  the chart and compute k c  = k/k ; r  or  (ii) one can estimate a value  of  к in
                                    r
                           the  low-density  region  by  the methods given  in §9.3 and the proceed  as  in  (i). Values  of
                           k  obtained by method  (i) are given in Appendix  E.
                            c
                              For  mixtures, one might estimate the thermal conductivity by  methods analogous  to
                           those described  in  §1.3. Very  little  is  known  about  the accuracy  of  pseudocritical  proce-
                           dures  as  applied  to thermal conductivity, largely because  there are  so  few  data  on  mix-
                           tures at elevated  pressures.


       EXAMPLE  9.2-1      Estimate  the thermal  conductivity  of  ethane at  153°F  and  191.9  atm  from  the  experimental
                               2
                           value  к = 0.0159 Btu/hr •  ft • F at: 1 atm and  153°F.
     Effect  of Pressure  on
     Thermal  Conductivity  SOLUTION
                           Since a measured  value  of  к is  known, we  use  method  (i). First we  calculate p r  and  T  at the
                                                                                                r
                           condition  of the measured  value:



                           From Fig. 9.2-1 we read k  = 0.36. Hence k  is
                                                            c
                                               r
                                                                      /  ' '
                                                    vr   §W   = a0442 Btu hr ft  F
                           At  153°F (T  = 1.115) and  191.9 atm (p  = 3.98), we read from the chart k  = 2.07. The predicted
                                                                                   r
                                                         r
                                    r
                           thermal conductivity is then
                                              к = k k c  = (2.07X0.0422) = 0.0914 Btu/hr • ft • F  (9.2-3)
                                                  r
                                                                             2
                           An observed  value  of  0.0453 Btu/hr •  ft • F has been reported.  The poor agreement shows that
                           one  should  not rely  heavily  on this  correlation  for  polyatomic  substances  nor  for  conditions
                           near the critical point.



                               1
                                In the vicinity  of the critical point, where the thermal conductivity  diverges,  it is customary to
                                              ъ
                           write к = к  + &k, where к  is the "background"  contribution and A/c is the "critical enhancement"
                                   ъ
                           contribution. The k  being  used  in the corresponding  states correlation is the background  contribution.
                                        c
                           For the behavior  of transport properties near the critical point, see J. V. Sengers and J. Luettmer
                           Strathmann, in Transport Properties of Fluids  (J. H. Dymond, J. Millat, and C. A. Nieto de Castro, eds.),
                           Cambridge  University  Press  (1995); E. P. Sakonidou, H. R. van den Berg, С A. ten Seldam, and
                           J. V. Sengers, /. Chem. Phys., 105,10535-10555 (1996) and 109, 717-736 (1998).
                               2
                                J. M. Lenoir, W. A. Junk, and E. W. Comings, Chem. Eng. Progr., 49, 539-542  (1949).
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