Page 437 - Book Hosokawa Nanoparticle Technology Handbook
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7.4 REMOVAL OF NANOPARTICLES                                                 FUNDAMENTALS

                           Elementary cause      Force field        Force field          Obstacle
                                                                   and obstacle


                                                                           ¨
                                                                          Š
                                                                           •
                                                                          á
                                                                          Q
                                                                         Obstacle           Obstacle
                                                                          áŠQ•¨
                                                                                              Š
                                                                                              á áŠQ•¨ • ¨
                                                                                              Q
                                                        F
                         Form
                         Collection efficiency    low                 middle             high
                         Pressure drop            low                 middle             high
                         Critical factor      • Deposition velocity  • Collision efficiency  • Pressure drop
                         for performance                         • Pressure drop
                                              • Thickner         • Venturi scrubber  • Filter press
                         Separator            • ESP              • Fibrous filter    • Bag filter
                                              • Cyclone          • Granular bed      • Membrane filter

                  Figure 7.4.1
                  Basic forms of particle separation.


                  Therefore, the migration velocities or displacement  10 2
                  of a particle per second due to the individual forces
                  gives the basis for the comparison of removal effi-                  p  = 1g  • cm −3
                  ciencies due to each force. In Fig. 7.4.2, migration                 electrostatic
                  velocities of particles due to various forces are  10
                                                                                       force V E
                  depicted against particle diameter at normal temper-                (V 0  = 1kV  • cm )
                                                                                               −1
                                                         3
                  ature and pressure for particle density of 1g/cm [1].
                  As seen from the figure, the velocities due to grav-  unipolar
                  ity, centrifugal force, and inertia monotonically  1  diffusion charging
                  decrease with decreasing particle diameter, suggest-   (Nt = 10 7 , ε p = ∞)
                  ing that the removal of nanoparticles with these              unipolar field charging
                  forces is difficult. On the contrary, the velocities due  10 −3  (E = 5kv, Nt = ∞ ,    p = ∞)
                  to Brownian diffusion and electrostatic forces   migration velocity (cm • s − 1 )  thermophoresis v r  (NaCl)
                  increase with decreasing particle diameter for parti-           k g /k 3  = 0.0041
                  cles less than 100 nm. This suggests that Brownian               dT  = 100K  • cm −1
                                                                                    dx
                  diffusion and electrostatic forces are most effective  10 −2  Brownian diffudion V B
                  in collecting nanoparticles.
                                                                                                gravity V g
                    Fig. 7.4.3 summarizes typical conventional dust
                  collectors. Among them, the effective collectors for                  centrifugal force V c  (Z=10)
                  nanoparticles are ESP and fabric/air filter. However,  10 −1  inertia V i
                  for the case of ESP, which relies on only electrostatic     = 340m  • s −1 )    inertia V i
                  force, nanoparticles ( 10nm) fail to carry even one                              (u = 1m  • s − 1 )
                  electron resulting in low collection efficiency. In this  −4  (u  0
                  case electrically charged filters are effective because  10  10  -3  10 -2  -1
                  we can expect the combined effects of electrostatic                  10        1       10
                  forces and Brownian diffusion.                                 particle diameter (μm)
                    Among charged filters, so-called electret filter,
                  which consists of permanently polarized fibers, is the  Figure 7.4.2
                  most favorable filter because of its charge stability.  Migration velocity of airborne particles under force fields.
                  Particle penetration data of electret filter are plotted
                  against particle diameter in Fig. 7.4.4 and compared  diameters. For the uncharged fiber, collection effi-
                  with that of uncharged filter with the same structure.  ciency of uncharged particle has a minimum at
                  For the three combinations of charged states of fiber  100 nm and increases with decreasing particle diam-
                  and particle there exist the most penetrating particle  eter, showing that 100 nm is the most penetrating

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