Page 62 - gas transport in porous media
P. 62

CHAPTER 5

                           TWO-PHASE GAS TRANSPORT





                           STEPHEN W. WEBB
                           Sandia National Laboratories, P.O. Box 5800, Albuquerque, NM 87185, USA


                           Chapter 2 was limited to all-gas conditions. This chapter addresses two-phase, or
                           unsaturated, gas transport in the presence of a liquid. While the same general transport
                           mechanisms (advection and diffusion) exist as discussed in Chapter 2, gas transport
                           under two-phase conditions must consider the influence of the liquid phase. Not only
                           does the liquid phase interfere with gas-phase transport in the gas phase, but gas
                           transport may occur in the liquid phase as a dissolved species. The presentation in
                           this chapter complements the discussion given in Chapter 2.
                             As in Chapter 2, energy transport is not discussed in this chapter. It is treated by
                           Plumb (Chapter 27 of this book), Nield and Bejan (1999), and Kaviany (1995).


                           5.1  GAS-PHASE ADVECTION

                           5.1.1  Darcy’s Law
                           Darcy’s law as presented in Section 2.1.1 is often extended to two-phase conditions
                           with separate equations for the gas and liquid phases. Relative permeabilities for each
                           phase are introduced into the momentum equations to account for the influence of the
                           other phase. Each phase may be at a different pressure due to interfacial curvature, so
                           a pressure relationship between the two phases (capillary pressure) is also included.
                             For unsaturated flow conditions, the Darcy equations for mass flux can be written as

                                                       k g k r,g
                                                F g =−      ρ g (∇P g − ρ g g)
                                                        µ g
                                                       k   k r,
                                                F   =−      ρ   (∇P   − ρ   g)
                                                        µ
                             The equation for the gas mass flux is the same as in Section 2.1.1 except for the
                           addition of the term k r,g , which is the gas-phase relative permeability. The relative
                                                            55
                           C. Ho and S. Webb (eds.), Gas Transport in Porous Media, 55–70.
                           © 2006 Springer.
   57   58   59   60   61   62   63   64   65   66   67