Page 245 - Soil and water contamination, 2nd edition
P. 245

232                                                  Soil and Water Contamination

                                                                             -1
                       During this time, the water has travelled a distance of 5702 s × 0.2 m s  = 8260 m. Thus,
                       the suspended sediment  concentration has diminished by 75 percent over a distance of
                       8260 m.
                    If the water flow around the particles is laminar , the settling velocity w  can be described by
                                                                            s
                    Stokes’s law . Stokes’s law assumes that the upward force according to Archimedes’ principle
                    and the shear stress es during settling are in equilibrium with the gravity force. For spherical
                    particles, Stokes’s law is:
                         1  (     ) g  d  2
                    w        s   w                                                    (12.16)
                     s
                        18       M
                                                             -3
                                                                                          -3
                    where  ρ  = the density of the solid particles [M L ],  ρ  = the density of water [M L ],
                          s                                      w
                                                              -1
                                                        -3
                                                                -1
                                                                         -1
                                                                       -1
                    μ = the dynamic viscosity  of water (= 1.14 10  kg m  s ) [M L  T ], g = the gravitational
                                               -2
                                                      -2
                    acceleration constant (= 9.8 m s ) [L  T ], and  d = the diameter of the particles. As
                    mentioned above, Equation (12.16) is only valid for laminar  flow around the particle. The
                    flow regime (laminar or turbulent flow ) is described by the Reynolds number . For flow
                    around the particles the Reynolds number is defined as:
                         w    d
                    Re     s  w                                                       (12.17)
                           M
                    where Re = Reynolds number  [-]. If the Reynolds number is sufficiently small (< 1) then the
                    flow around the particles is laminar . If the Reynolds number is greater than 1 (in general,
                    this is the case for particles larger than about 100–150 μm) then the settling velocity can be
                    approximated by (Fair et al., 1968):
                           4  (  s   w )  g  d                                        (12.18)
                    w
                     s
                          3  C  d   w
                    where C  = the Newton’s drag coefficient [-], which is estimated by:
                          d
                         24    3
                    C d              . 0  34                                          (12.19)
                         Re    Re
                    If the Reynolds number  exceeds 2000 (in general, this is the case for solid particles larger
                    than about 1.4 mm), then C  becomes independent of Re. In this case, the settling velocity
                                           d
                    can be approximated by:
                    w      3 . 3  (  s  w  )  g  d                                    (12.20)
                     s
                    Particles that are not spherical have a somewhat slower settling velocity (up to a factor of
                    about 1.4 less).
                       As can be seen from Equations (12.16), (12.18), and (12.20), the settling velocity
                    depends on both the diameter and the specific density of the particles. Considering the
                    variety in the nature and size of the particles, it is practically impossible to formulate one

                    mass balance  for all suspended matter . Usually, suspended matter is subdivided on the basis
                    of the nature and size of the particles, or a mass balance is formulated for the most abundant
                    class of suspended matter. Apart from that, the particle size distribution and densities of
                    the particles in natural waters are difficult to measure directly. An important feature of fine
                    particles is that they tend to coagulate to form flocs. The flocculation  process occurs if the
                    thickness of the ‘diffuse layer ’ surrounding the particle, which is governed by the chemical
                    composition of the water, decreases, enabling the particles to approach each other more
                    closely (see Section 4.2.3). The flocculation process is also favoured by the presence of sticky










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