Page 504 - Bird R.B. Transport phenomena
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484   Chapter 15  Macroscopic Balances  for Nonisothermal Systems

                           The quantity У represents the ratio of the heat transferred  in the "1-2 parallel-counterflow  ex-
                           changer"  shown  to that transferred  in a true counterflow  exchanger  of  the same area and ter-
                           minal  fluid  temperatures. Values  of  Y(R, 4?) are  given  graphically  in  Perry's  handbook.  2  It
                           may be seen that Y(R, 40  is always less than unity.
                     15C.2.  Discharge  of  air from  a large tank.  It is desired  to withdraw  5 lb /s from a large storage tank
                                                                               m
                           through an equivalent  length  of 55 ft  of new steel pipe 2.067 in. in diameter. The air undergoes
                           a  sudden  contraction on entering  the pipe, and  the accompanying  contraction loss  is  not in-
                           cluded  in the equivalent  length  of  the pipe. Can the desired flow rate be obtained  if  the air in
                           the tank is at 150 psig and 70°F and the pressure at the downstream  end  of the pipe is 50 psig?
                               The effect  of the sudden  contraction may  be estimated  with  reasonable  accuracy by con-
                           sidering  the entrance to consist  of  an ideal  nozzle converging  to a cross  section equal  to that
                           of  the pipe, followed  by  a section  of  pipe with  e v  = 0.5  (see Table  7.5-1). The behavior  of  the
                           nozzle  can be determined  from  Eq. 15.5-34 by  assuming  the cross  sectional  area S^  to be  infi-
                           nite and Q  to be unity.
                           Answer: Yes.  The calculated  discharge  rate is  about 6 lb /s  if  isothermal flow is  assumed  (see
                                                                        m
                           Problem  15B.3) and about 6.3 lb /s  for adiabatic flow. The actual rate should be between  these
                                                    m
                           limits for an ambient temperature of  70°F.
                     15C.3.  Stagnation temperature  (Fig. 15C.3).  A  "total temperature probe,"  as  shown  in the figure,  is
                           inserted  in a steady  stream  of  an ideal  gas  at a temperature  7^ and moving  with  a velocity  v v
                           Part of the moving  gas  enters the open end of the probe and is decelerated to nearly zero veloc-
                           ity before  slowly leaking  out of the bleed  holes. This deceleration results  in a temperature rise,
                           which is measured by the thermocouple. Since the deceleration is rapid, it is nearly adiabatic.
                           (a)  Develop an expression  for  the temperature registered  by  the thermocouple in terms  of Т л
                           and Vi by using  the steady-state  macroscopic energy  balance, Eq. 15.1-3. Use as your system a
                           representative  stream  of  fluid  entering  the  probe.  Draw  reference  plane  1  far  enough  up-
                           stream that conditions may be assumed  unaffected  by  the probe, and reference  plane 2 in the
                           probe  itself. Assume  zero  velocity  at  plane  2, neglect  radiation, and  neglect  conduction  of
                           heat from  the fluid as it passes between  the reference  planes.
                           (b)  What  is the function  of the bleed  holes?
                           Answer: (a) T 2  -  T }  = v\/2C r  Temperature rises  within  about  2%  of  those given  by  this  ex-
                           pression  and may be obtained with well-designed  probes.

                    15D.1.  The macroscopic entropy balance.
                           (a)  Show  that integration  of  the equation  of  change  for  entropy  (Eq.  11D.1-3)  over  the flow
                           system  of  Fig. 7.0-1 leads to
                                                             ,  Я
                                                                    + gstoi + Qs              (15D.1-1)
                           in  which
                                                   >  = j  pSdV                               (15D.1-2)
                                                    tot

                                                                    T)  +  (T:VV)WV           (15D.1-3)


                                    No. 30 I-C thermocouple
                               Steel    0.025" sphere
                                 I     /
                             F                             ~T     I
                                                  -0.25"-  0.071"  0.095"
                                         _L
                                                                        Fig. 15C.3.  A "total temperature
                               Plastic  Three 0.023" bleed holes        probe."  [H. C. Hottel and A. Kalitin-
                                         equally  spaced                sky,  /. Appl. Mech., 12, A25  (1945).]
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