Z. angew. Math. Phys. 51 (2000) 481–490 0044-2275/00/030481-10 $ 1.50+0.20/0 c 2000 Birkhäuser Verlag, Basel Zeitschrift für angewandte Mathematik und Physik ZAMP Stokes flow inside a porous spherical shell G. P. Raja Sekhar and T. Amaranath Abstract. Stokes flow of a viscous, incompressible fluid inside a sphere with internal singularities, enclosed by a porous spherical shell, using Darcy’s law for the flow in the porous region is discussed. The formulae for drag and torque are found by deriving the corresponding Faxen’s laws. It is found that torque does not depend on the thickness of the spherical shell. Mathematics Subject Classification (1991). 76D07. Keywords. Stokes flow, Darcy law, porous spherical shell. 1. Introduction Interest in flow past spherical boundaries began with the pioneering work of Hasimoto [1] who discussed axisymmetric flow past a rigid sphere. Subsequently several papers ( Shail [2], Collins [3], Palaniappan [4]) appeared on this topic. Recently an interesting review of Stokes flows past spherical boundaries is due to Hasimoto [5]. Palaniappan et al. [4] proposed a solution for Stokes equations. This solution was shown to be a complete general solution by Raja Sekhar et al. [6]. Here we use this solution to discuss the problem of a non-axisymmetric Stokes flow of a viscous, incompressible fluid inside a sphere of radius ‘b’ with internal singularities, enclosed by a porous spherical shell of thickness (a − b) with an impermeable outer boundary. We assume that the flow in the porous region obeys Darcy law [7] and the flow inside the liquid sphere obeys Stokes equations. We assume that the flow is generated by singularities inside the clear fluid region, as in the absence of body forces fluid flow can be generated by the presence of such singularities. One has to impose suitable boundary conditions at the interface of clear fluid and porous region. Several types of boundary conditions were suggested in literature. Beavers and Joseph [8] have proposed an empirical slip flow condition for a plane boundary. In the limit of small permeability, Saffman [9] gave a theoretical justification for the empirical boundary condition proposed by Beavers and Joseph [8]. In the limit k → 0, where k represents permeability they showed that one can derive the 482 G. P. Raja Sekhar and T. Amaranath ZAMP √ k du + O(k) α dn at the interface, where u is the tangential velocity and n is measured along the normal to the interface and this result is consistent with that of Beavers and Joseph. The theoretical and experimental evidence supported the view that the Darcy equation offers a good representation of the flow in many low porosity systems and therefore for relatively small permeabilities. In light of this, Saffman’s condition has gained considerable importance. Recently Ochoa - Tapia and Whitaker ([10], [11]) suggested a stress jump boundary condition at the fluid/porous interface. They have used the Brinkman - extended Darcy law and shown that the process of matching the Brinkman extended Darcy law to the Stokes equations requires a discontinuity in the stress. Kuznetsov ([12], [13], [14]) has used the stress jump boundary condition at the interface between a porous medium and a clear fluid to discuss flow in channels partially filled with a porous medium. We shall use the Saffman [9] condition together with continuity of the normal velocity component and pressure at the permeable boundary, as we are using Darcy law for the porous region and not the Brinkman extended Darcy law. We also discuss some physical properties like drag and torque by deriving the corresponding Faxén’s [15] laws. condition u= 2. Mathematical formulation Let us consider an arbitrary Stokes flow of a viscous, incompressible fluid inside a sphere of radius ‘b’ with internal singularities, enclosed by a porous spherical shell of thickness (a − b). The flow inside the region r < b is governed by the Stokes equations µ∇2 Vi = ∇pi , ∇.Vi = 0, (1) (2) where µ is the coefficient of viscosity, Vi the velocity and pi the pressure of the fluid. The superscript ‘i’ denotes the flow inside the region (r < b). Similarly, we use the superscript ‘e’ for the flow inside the porous region (b ≤ r ≤ a). The velocity components of Vi in spherical polar coordinates are qri , qθi and qϕi . The flow inside the porous region (b ≤ r ≤ a) is governed by the Darcy’s law k (3) Ve = − ∇pe , µ ∇.Ve = 0, (4) where Ve is the volume rate of flow per unit cross section area, pe the pressure and k > 0 is the permeability coefficient. The velocity components of Ve in spherical polar coordinates are qre , qθe and qϕe . Vol. 51 (2000) Stokes flow inside a porous spherical shell 483 3. Boundary conditions The boundary conditions are assumed to be as follows: a) the pressure is continuous on r = b pe (b, θ, ϕ) = pi (b, θ, ϕ), (5) b) the normal component of the velocity is continuous on the boundary of the shell r=b qre (b, θ, ϕ) = qri (b, θ, ϕ), (6) c) Saffman’s conditions for the tangential components of velocity on the shell are satisfied on r = b √ ∂q i k θ (b, θ, ϕ), ∂r i √ ∂q ϕ qϕi (b, θ, ϕ) = k (b, θ, ϕ), ∂r qθi (b, θ, ϕ) = (7) (8) d) the normal component of velocity vanishes on r = a qre (a, θ, ϕ) = 0, (9) 4. Method of solution We assume the representation proposed by Palaniappan et al. [4] for the velocity and pressure in the region r < b, given by Vi = CurlCurl(rAi ) + Curl(rB i ), ∂ pi = p0 + µ (r∇2 Ai ), ∂r (10) (11) where ∇4 Ai = 0, ∇2 B i = 0 and p0 is a constant. Suppose the basic flow is given by A0 (r, θ, ϕ) = B0 (r, θ, ϕ) = ∞ X n=1 ∞ X n=1 αn rn+1 χn rn+1 0 αn + n− r 1 Tn (θ, ϕ), ! Sn (θ, ϕ), (12) (13) 484 G. P. Raja Sekhar and T. Amaranath ZAMP where Sn (θ, ϕ) = Tn (θ, ϕ) = n X m=0 n X Pnm (ζ)(Anm cos mϕ + Bnm sin mϕ), (14) Pnm (ζ)(Cnm cos mϕ + Dnm sin mϕ), (15) m=0 0 and ζ = cos θ, Pnm is the associated Legendre polynomial, αn , αn , χn , Anm , Bnm , Cnm and Dnm are known constants. The expansions given in (12) and (13) are valid in the region 0 < c < r < b and we shall explain in specific examples how these expansions occur. These expansions are used after adding the necessary perturbed terms to satisfy the boundary conditions on r = b. Also A0 and B0 given in the equations (12) and (13) satisfy the expressions ∇4 A0 = 0 and ∇2 B0 = 0. Now, in presence of the rigid boundary r = a and the permeable boundary r = b, the region of thickness (a − b) being porous, the modified flow is assumed in the region r < b as follows ! 0 ∞ X 0 α α n n Ai = + n− + βn rn + βn rn+2 Sn (θ, ϕ), (16) rn+1 r 1 Bi = n=1 ∞ X n=1 χn rn+1 + σn rn Tn (θ, ϕ) (17) and the pressure in the porous region (b < r < a) is assumed as pe = p0 + ∞ X r n n + n=1 0 0 Sn (θ, ϕ), n+1 n 1 r (18) 0 where βn , βn , σn , n and n are unknown constants to be determined from the boundary conditions. The modified flow given in (16) - (17) is assumed by adding the perturbed terms to the basic flow (12) - (15). The form of Ai and B i ensures that they satisfy ∇4 Ai = 0 and ∇2 B i = 0 respectively and that the perturbed terms vanish as r → 0. Using the scalar functions Ai and B i given in equations (16) - (17), the velocity components and pressure given in (18) for the modified flow inside the region (r < b) become qri = ∞ X h 0 n(n + 1) αn r−(n+2) + αn r−n n=1 i 0 + rn−1 βn + rn+1 βn Sn (θ, ϕ), qθi = ∞ h X n=1 (19) 0 −nr−(n+2) αn − (n − 2)r−n αn + (n + 1)rn−1 βn Vol. 51 (2000) Stokes flow inside a porous spherical shell 0 + (n + 3)rn+1 βn ∞ h X qϕi = i ∂S h i ∂T n + csc θ χn r−(n+1) + σn rn , ∂θ ∂ϕ n 485 (20) 0 −nr−(n+2) αn − (n − 2)r−n αn + (n + 1)rn−1 βn n=1 i i ∂T 0 ∂Sn h n − χn r−(n+1) + σn rn , + (n + 3)rn+1 βn csc θ ∂ϕ ∂θ ∞ h X 0 pi = p0 + 2µ n(2n − 1)r−(n+1) αn (21) n=1 i 0 + (n + 1)(2n + 3)rn βn Sn (θ, ϕ). (22) For the porous region (b < r < a) from the equations (3) and (18) the components of volume rate of flow and the pressure are given respectively by qre = − qθe = − ∞ i 0 k X h n−1 nr n − (n + 1)r−(n+2) n Sn (θ, ϕ), µ k µ n=1 ∞ h X 0 rn−1 n + r−(n+2) n n=1 i ∂S n ∂θ , i ∂S Xh 0 k n = − csc θ rn−1 n + r−(n+2) n , µ ∂ϕ (23) (24) ∞ qϕe (25) n=1 pe = p0 + ∞ X 0 rn n + r−(n+1) n Sn (θ, ϕ). (26) n=1 The expressions given in equations (19) - (26) satisfy the boundary conditions given in equations (5) - (9) if 0 0 (An αn + An αn ) , Ln 0 0 (Bn αn + Bn αn ) = , Ln 0 0 (Cn αn + Cn αn ) = , Ln 0 0 (Cn αn + Cn αn ) n = a2n+1 , n+1 Ln √ [b + (n + 1) k]χn √ =− , [b − n k]b2n+1 βn = 0 βn n 0 n σn where h √ An = −(2n + 3) b2 (b − k) na2n+1 + (n + 1)b2n+1 (27) (28) (29) (30) (31) 486 G. P. Raja Sekhar and T. Amaranath i √ + 2n(n + 1)k(b + (n + 2) k) b2n+1 − a2n+1 , h √ 0 An = −(2n + 1) b4 (b − 3 k) na2n+1 + (n + 1)b2n+1 i √ 2n+1 + 2kb2 2(n2 + n − 3)b − 3n(n + 1) k b − a2n+1 , √ Bn = (2n + 1)(b + k) na2n+1 + (n + 1)b2n+1 , h √ 0 Bn = (2n − 1) b2 (b − k) na2n+1 + (n + 1)b2n+1 i √ + 2n(n + 1)k(b − (n − 1) k) b2n+1 − a2n+1 , √ Cn = 2(n + 1)2 (2n + 1)(2n + 3)µ(b + k)b2n+1 , h √ i 0 Cn = 2(n + 1)(2n − 1)(2n + 1)µ b(n + 3) − 3(n + 1) k b2n+3 , h √ Ln = 2b2n+1 b2 (b − 2(n + 1) k) na2n+1 + (n + 1)b2n+1 i √ − (n + 1)2 (2n + 3)k(b − (n − 1) k)(b2n+1 − a2n+1 ) . ZAMP (32) (33) (34) (35) (36) (37) (38) 5. Faxén’s laws for a porous spherical shell Faxén’s [15] laws provide expressions for the drag and torque acting on the rigid sphere of radius ‘a’ in an unbounded, arbitrary Stokes flow. We now give the corresponding Faxén’s laws for the porous spherical shell. These expressions enable us to calculate the drag D and the torque T from the basic velocity directly. The force D exerted on the porous spherical shell by the fluid in the region r < b is found to be ! √ (b + k)(a3 + 2b3 ) 6πµ √ [Vo ]0 D=− 3 b [b2 (b − 4 k)(a3 + 2b3 ) − 20kb(b3 − a3 )] ! √ πµ [b2 (b − k)(a3 + 2b3 ) + 4kb(b3 − a3 )] √ − 3 [∇2 Vo ]0 , (39) 5b [b2 (a3 + 2b3 )(b − 4 k) − 20kb(b3 − a3 )] and the torque T on the shell is 4πµ T= 3 b √ ! 3 k √ 1+ [∇ × Vo ]0 , b− k (40) where Vo is the velocity corresponding to the basic flow and [ ]0 is evaluation at the origin r = 0. Vol. 51 (2000) Stokes flow inside a porous spherical shell 487 6. Examples (i). Stokeslet Consider a Stokeslet of strength F1 /8πµ located at (0, 0, c), (c < b < a) whose axis is along the positive direction of the x-axis. The corresponding expressions for A0 and B0 due to the Stokeslet are F1 cos ϕ (r cos θ − c + R1 ) , 8πµc r sin θ F1 sin ϕ (r cos θ − c + R1 ) , B0 = 8πµc r sin θ A0 = (41) (42) where R12 = r2 + c2 − 2rc cos θ. The expressions for A0 and B0 given in (41) and (42) are expanded in terms of spherical harmonics. These expansions are valid for 0 < c < r and are given by A0 = ∞ F1 X cn−1 (n + 3)cn+1 [ n−1 − ]P 1 (ζ) cos ϕ, 8πµ r n(n + 1) n(n + 1)(2n + 3)rn+1 n n=1 B0 = F1 8πµ ∞ X n=1 (43) n c P 1 (ζ) sin ϕ. rn+1 n(n + 1) n (44) The drag and torque are obtained using the formulae (39) and (40) as follows ! √ 3c2 (b + k)(a3 + 2b3 ) √ D= 3 F1 î 5b [b2 (b − 4 k)(a3 + 2b3 ) − 20kb(b3 − a3 )] ! √ 1 [b2 (b − k)(a3 + 2b3 ) + 4kb(b3 − a3 )] √ − 3 F1 î, (45) 2b [b2 (b − 4 k)(a3 + 2b3 ) − 20kb(b3 − a3 )] √ ! c 3 k √ F1 ĵ. (46) T= 3 1+ 2b b− k Since Darcy’s law is supposed to be valid for small values of permeability, the variation of drag and torque with the permeability is shown graphically for the range 0 ≤ k ≤ 0.04 cm2 . The graphs are plotted for the values c = 0.5cm, a = 2cm, b = 1cm and F1 = 1dyne. (ii). Rotlet Consider a rotlet of strength F2 /8πµ at (0, 0, c),(c < b < a) whose axis is along the positive y-axis direction. The corresponding expressions for A0 and B0 due to the rotlet are F2 cos ϕ (r cos θ − c + R1 ) , 8πµc r sin θ F2 sin ϕ B0 = − (r cos θ − c + R1 ) , 8πµcR1 r sin θ A0 = − (47) (48) 488 G. P. Raja Sekhar and T. Amaranath ZAMP 0.45 torque drag –0.25 –0.30 –0.35 0.40 0.35 0.30 –0.40 0.25 0.00 0.01 0.02 0.03 0.04 permeability variation of torque for Stokeslet 0.00 0.01 0.02 0.03 0.04 permeability variation of drag for Stokeslet 0.56 0.54 0.52 0.50 0.48 0.46 0.44 0.42 0.40 torque drag Figure 1. 0.00 0.01 0.02 0.03 0.04 permeability variation of drag for Rotlet 1.8 1.7 1.6 1.5 1.4 1.3 1.2 1.1 0.00 0.01 0.02 0.03 0.04 permeability variation of torque for Rotlet Figure 2. y P (0, 0, c): Location of the singularity on z-axis L: Liquid region P: Porous region L x (0, 0, c) z Figure 3. where R12 = r2 + c2 − 2rc cos θ Vol. 51 (2000) Stokes flow inside a porous spherical shell 489 The corresponding expressions in series form for 0 < c < r are ∞ F2 X cn A0 = − P 1 (ζ) cos ϕ, 8πµ rn+1 n(n + 1) n B0 = − F2 8πµ n=1 ∞ X n=1 cn−1 1 P (ζ) sin ϕ. rn+1 n n (49) (50) The drag and torque are obtained using the formulae (39) and (40) as follows 3c D= 3 4b T= 1 b3 ! √ (b + k)(a3 + 2b3 ) √ F2 î, b2 (b − 4 k)(a3 + 2b3 ) − 20kb(b3 − a3 ) √ ! 3 k √ F2 ĵ. 1+ b− k (51) (52) For the values c = 0.5cm, a = 2cm, b = 1cm and F2 = 1dyne, the variation of drag and torque with permeability is shown graphically in Fig.2 (i) and Fig.2(ii) respectively for the range 0 ≤ k ≤ 0.04cm2 . In Fig.2(i), it is seen that the drag decreases in magnitude and is in the negative x-direction. The expressions given for A0 and B0 in equations (43) and (44) for a Stokeslet at (0, 0, c) and (49) and (50) for a rotlet at (0, 0, c) respectively are what we have presented in equations (12) and (13) in a general case, which are valid in c < r. Conclusions We have discussed a non-axisymmetric Stokes flow inside a sphere of radius b bounded by a porous spherical shell of thickness (a − b). The flow is generated by the presence of singularities inside the sphere as, in absence of body forces fluid flow can be generated by singularities. Expressions for drag and torque are presented in equations (39) and (40) respectively. It can be observed from equation (40) that torque is always greater than that corresponding to a rigid sphere. It does not depend on the thickness of the shell. Torque depends on the permeability and increases with permeability. This fact can be observed from the figures (fig. 1(i) , fig. 2(i)) in the case when the flow is generated by a Stokeslet and a rotlet respectively. However, drag behaves differently. In the case of a Stokeslet drag first increases and then decreases in magnitude in the -ve x direction with increasing permeability (fig. 1(ii)). Whereas drag increases first and then decreases in magnitude in the +ve x direction with increasing permeability (fig. 2(ii)) in the case of a rotlet. 490 G. P. Raja Sekhar and T. Amaranath ZAMP Acknowledgements The authors thank the referees for their constructive suggestions on their earlier version which have helped them to improve the presentation and in particular for bringing to their attention the works of Ochoa-Tapia and Whitaker and Kuznetsov. References [1] [2] [3] [4] [5] [6] [7] [8] [9] [10] [11] [12] [13] [14] [15] Hasimoto, H. J. Phys. Soc. Japan 7 (1956), 793–797. Shail, R., QJMAM 40 (1987), 223–233. Collins, W. D, Mathematika 5 (1958), 118–121. Palaniappan, D., T. Amaranath, S. D. Nigam and R. Usha, QJMAM 45 (1992), 47–56. Hasimoto, H., J. Engg. Maths. 30 (1996), 215. Raja Sekhar, G. P., B. S. Padmavathi and T. Amaranath, QJMAM (1998), (to appear). Darcy, H.P.G., Les Fontaines Publiques de la Ville de Dijon, Victor Dalmont, Paris 1856. Beavers, G. S and Joseph, D. D., J. Fluid Mech. 30 (1967), 197–207. Saffman, P. G., Stud. appl. Math. 50 (1971), 93–101. Ochoa-Tapia, J. A. and S. Whitaker Int. J. Heat and Mass Transfer 38 (1995), 2635–2646. Ochoa-Tapia, J.A and S. Whitaker Int. J. Heat and Mass Transfer 38 (1995), 2647–2655. Kuznetsov, A. V., Applied Scientific Research 56 (1996) 53–67. Kuznetsov, A. V, Int. J. Heat and Mass Transfer 24 (1997), 401–410. Kuznetsov, A. V, Int. J. Heat and Mass Transfer 41 (1998), 2556–2560. Faxén, Arkiv Mat. Atron. Fys. 18 (1924), 3. G. P. Raja Sekhar and T. Amaranath Department of Mathematics & Statistics University of Hyderabad Hyderabad - 500 046 India e-mail: tasm@uohyd.ernet.in (Received: May 26, 1998; revised: September 28, 1998)