Page 69 - Air pollution and greenhouse gases from basic concepts to engineering applications for air emission control
P. 69

2.1 Gas Kinetics                                                43

                                                                   2
              Then, the net flux of molecules in the positive x direction (#/s m )is
                                                  1 dC N
                                 J x ¼ J !x   J  x ¼   k  c              ð2:62Þ
                                                  3 dx
              Comparing this equation with the Fick’s law of diffusion

                                               dC N
                                       J x ¼ D                           ð2:63Þ
                                                dx
                                                         2
            gives the diffusivity or diffusion coefficient of gas in m /s:
                                             1
                                         D ¼ k  c                        ð2:64Þ
                                             3
              Combining with Eqs. (2.7) and (2.51), we can get leads to

                                         r ffiffiffiffiffiffiffiffi        r ffiffiffiffiffiffi
                              1    RT      8kT     2   RT    RT
                          D ¼ p  ffiffiffi           ¼               :         ð2:65Þ
                                                   1:5 2
                              3  2pN a d P  pm   3p d PN a   M
                                       2
            2.1.10 Viscosity of a Gas

            Viscosity is a measure of the resistance of a fluid being deformed by either shear or
            extensional stress. Viscosity in gases arises principally from the molecular diffusion
            that transports momentum between layers of flow. The kinetic theory of gases
            allows accurate prediction of the viscosity of a gas.
              Similar to the analysis for diffusivity, consider a laminar flow of gas above a
            horizontal plate. We can apply finite element analysis from x   kÞ to x þ kÞ. The
                                                                    ð
                                                            ð
            concentration at x is C N . Assuming a constant gas velocity gradient of  du  from
                                                                        dx

                                            ð
            ð x   kÞ to x þ kÞ; the velocities at x þ kÞ and x   kÞ are  u þ  du  k  and
                                                       ð
                     ð
                                                                      dx

                du
             u    k , respectively. The gas may be treated as layers perpendicular to the
                dx
            moving direction (say x axis). Also assume a constant gas molecule concentration
            C N . In each layer, the steady flow gas velocity is also constant. Then, the rate of
            transport of momentum per unit area in the þx and  x directions, respectively, are

                                        1          ou
                                  M !x ¼ C N m  cu    k
                                        6          ox
                                        1          ou
                                  M  x ¼ C N m  cu þ  k
                                        6          ox
   64   65   66   67   68   69   70   71   72   73   74