Page 549 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
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     504                            Fundamentals of Water Treatment Unit Processes: Physical, Chemical, and Biological
                          (a)                                  (b)
            FIGURE G15.1 GC-MS instrument for volatile organic compounds. (a) Left-to-right: GC-MS, purge-and-trap unit, auto-sampler, com-
            puter. (b) Column for GC, 60 m length, 0.32 mm i.d., 1.8 mm silicon film. (Courtesy of Klein Water Treatment Facility, Commerce City, CO,
            2003, with cooperation of Charlene Seedle.)
                   concentration at a given temperature. (2) The adsorp-  tion and at the surface of the particle. The mass
                   tion reaction is always between particular adsorbate  transfer coefficient is designated, k f .
                   and a particular adsorbent, resulting in a particular  Pore diffusion model: The pore diffusion model neglects the
                   equilibrium constant. The equilibrium equation may  mechanism of surface diffusion. The pore–diffusion
                   be manipulated to give a mathematical relationship  coefficient is designated, D p .
                   called an isotherm whose constants are unique  Homogeneous surface diffusion model: The homogeneous
                   for the particular adsorbate–adsorbent reaction. The  surface diffusion model is identical to the pore–sur-
                   relation is called an ‘‘isotherm’’ because it is valid for  face diffusion model except that intra-particle pore
                   only a particular temperature (i.e., the equilibrium  diffusion is considered negligible compared to sur-
                   constant, the isotherm constants, and the associated  face diffusion. The surface–diffusion coefficient is
                   graphical depiction). [The temperature effect is   designated, D s .
                   described by the well-known van’t Hoff equation      [See also Weber and DiGiano (1996) for further
                   (see Section 15.2.1.2).]                           explanations.]
            Kinetics: A term that refers to the rate of change of a given  Langmuir isotherm: An equilibrium relationship between
                   reactant with respect to time. With reference to   adsorbate and adsorbent as defined for a given
                   adsorption, kinetics refers to the rate of uptake of  temperature.
                   adsorbate by the adsorbent.                 Linearized Langmuir isotherm: An algebraic rearrange-
            Kinetic theory: The most common kinetic models are        ment of the Langmuir relation can yield a linear
                   (adapted from Carter and Weber, 1994, p. 614)      relationship between variables that is useful in deter-
                   (1) the pore-surface diffusion model and its two   mining the constants, a and X m , from experimental
                   major derivatives: (a) the pore diffusion model, and  data of (C*, X*) pairs. At least three variations of
                   (b) the homogeneous surface diffusion model. These  such relationships are possible.
                   models are described as follows:            London dispersion forces: (1) A subset of van der Waals
            Pore-surface diffusion model: The pore-surface diffusion  forces defined by F. London in 1930. ‘‘The force is
                   model incorporates a mathematical description of   always attractive and arises from fluctuating electron
                   the major physicochemical mechanisms involved      clouds in all atoms that appear as oscillating dipoles
                   in the adsorption of an adsorbate from the flowing  created by the positive nucleus and negative
                   solution and into the adsorbate particles. These   electrons.’’ (Adamson and Gast, 1997, p. 228).
                   mechanisms include axial flow (i.e., advection      (2) ‘‘London developed a quantum mechanical
                   within the reactor), hydrodynamic dispersion, local  perturbation theory according to which the continu-
                   equilibrium at the particle surface, mass-transfer  ous motion of electrons in atoms and molecules
                   resistance across the hydrodynamic boundary layer  effect rapidly fluctuating temporary dipole and quad-
                   (known as the ‘‘film’’) surrounding the particle,   rupole moments. Such fluctuating dipole and quad-
                   and intra-particle diffusion along the pore surfaces  rupole moments in foreign molecules or atoms
                   and through the pore solution within the particle.  approaching a solid surface can perturb the electron
                   The surface–diffusion coefficient is designated, D s .  distribution of surface molecules to induce tempor-
            Film diffusion model: The film diffusion model depicts dif-  ary dipoles and quadrupoles therein, and conversely.
                   fusion across the boundary layer in terms of the   This leads to extensive permutation of induced
                   concentration differential between the bulk of solu-  and temporary dipole-dipole, dipole-quadrupole and
     	
