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               178                                                                              Mass Transfer and Diffusion


               fluid-fluid interfaces. They describe mass transfer from a  TABLE III Common Forms of Mass Transfer Coefficients
               liquid to a gas or from one liquid to another liquid. Heat
                                                                    Basic    Typical units
               transfer coefficients normally describe transport from a  a         b
                                                                  equation     of k              Remarks
               solid to a fluid. This makes the analogy between heat and
               mass transfer less useful than it might at first seem.  N 1 = k  c 1  cm/sec  Common in the older literature;
                 The correlations in Table II are most often written in                   used here because of its
                                                                                          simple physical significance
               dimensionless numbers. The mass transfer coefficient k,              2
               which most frequently has dimensions of velocity, is in-  N 1 = k p  p 1  mol/cm -sec  Common for a gas absorption;
                                                                               − atm      equivalent forms occur
               corporated into a Sherwood number Sh                                       in biological problems
                                                                                   2
                                       kd                         N 1 = k x  x 1  mol/cm -sec  Preferred for practical calculations,
                                  Sh =                   (35)                             especially in gases
                                        D
                                                                 Ni = k c 1   cm/sec    Used in an effort to include
               where d is some characteristic length, like a pipe diameter  + c 1 v 0     diffusion-induced convection
               or a film thickness, and D is the same diffusion coeffi-
                                                                                                     2
                                                                        a
               cient which we talked about earlier. The mass transfer  Notes: In this table, N 1 is defined as moles/L t, and c 1 as
                                                                       3                                 2
               coefficient is most frequently correlated as a function of  moles/L . Parallel definitions where N 1 is in terms of M/L t and c 1
                                                                      3
                                                                 is M/L t are easily developed. Definitions mixing moles and mass are
               velocity, which often appears in a Reynolds number Re  infrequent.
                                       dv                          b  For a gas of constant molar concentration c, k = RT k p = k y /c.For
                                  Re =                   (36)    a dilute liquid solution k = (M 2 /ρ)k x , where M 2 is the molecular weight
                                        ν
                                                                 of the solvent, and ρ is the solution density.
               where v is the fluid velocity and ν is the kinematic viscos-
               ity; in a Stanton number St
                                                                 in a gas phase which was an equilibrium with the blood at
                                        k                        the experimental conditions.
                                   St =                  (37)
                                        v                          Each of these units of concentration may be used to
               or as a Peclet number Pe                          define a different mass transfer coefficient, as exemplified
                                                                 by the definitions in Table III. It is not a difficult task to
                                       dv
                                  Pe =                   (38)    convert a value from one form of coefficient into another
                                        D
                                                                 form of coefficient (Cussler, 1997; Treybal, 1980). How-
               The variation of mass transfer coefficients with other pa-  ever, it is complicated and requires care. It’s like balancing
               rameters, including the diffusion coefficient, is often not  a check book: it doesn’t always work out the first time you
               well studied, so the correlations may have a weaker exper-  try it. Still, we normally find that with the definitions like
               imental basis than their frequent citations would suggest.  those in Table III held firmly in mind, we can readily con-
                                                                 vert from one form of coefficient to another.
                                                                   The second reason that mass transfer coefficients are
               B. Problems with Mass Transfer Coefficients
                                                                 considered difficult happens when mass transfer occurs
               Mass transfer coefficients are frequently regarded as a  from one fluid phase into another. This is a genuine source
               difficult subject, not because the subject is inherently  of difficulty, where confusion is common. To see why the
               difficult, but because of different definitions and be-  difficulty occurs, imagine we are extracting bromine from
               cause of complexities for mass transfer from one solution  water into benzene. When we begin, the bromine is at
               into a second solution. These differences merit further  a higher concentration in the water than in the benzene
               discussion.                                       (Cussler, 1997). Later on, the concentrations in water and
                 The complexities of definitions occur primarily because  benzene become equal. Still later, the concentration in the
               concentration can be expressed in so many different vari-  water will have dropped well below that in the benzene.
               ables. In the above, we have assumed that it is expressed in  Even then, bromine can still be diffusing from its low con-
               mass per volume or moles per volume. The concentration  centration in the water into its much higher concentration
               can equally be well expressed as a mole fraction, which  in the benzene.
               in the liquid phase is commonly indicated by the symbol  The reason that this occurs is that bromine is much more
               x 1 and in a gas phase is written as y 1 . In gases, one can  soluble in benzene than it is in water. It partitions from
               also express concentrations as partial pressures. In some  water into benzene. At equilibrium, the concentration in
               cases, especially in medicine, the concentration can be ex-  benzene divided by that in water will be a constant much
               pressed in other more arcane units. For example, “oxygen  greater than one, and almost independent of the initial
               tension” measures the amount of oxygen present in blood,  concentration of the bromine in the water. Phrased in other
               but it is expressed as the partial pressure that would exist  terms, in the eventual equilibrium, the concentrations are
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