Applied Mathematical Sciences, Vol. 6, 2012, no. 123, 6137 - 6146 On the Two Immiscible Fluids in Contact with Each Other on a Solid Boundary Hishyar Kh. Abdullah Dept. of Mathematics, University of Sharjah Sharjah, P.O. Box 27272, UAE [email protected] Abstract. In this paper class of two immiscible ‡uids in contact with each other on a solid boundary, have been studied: The asymptotic solution near contact line is …ned for two cases. First we assume that the external gas has no e¤ect, then the case of external gas is assumed process viscosity comparable to that of the ‡uid. Mathematics Subject Classi…cation: 34C55, 76D05, 76D07, 76D08, 76D10 Keywords: Rayleigh-Ritz method, Fourier series expansion, Inclined rivulet 1. Introduction Immiccible ‡uids ‡owing over an undulating solid represent an everday physical phenomenon that has eluded accurate continuum description so far. At the heart of this probblem is the boundary condition for the moving contact line (MCL), de…ned as the intersection of the ‡uid-‡uid interface with the solid wall. The no-slip boundary condition, i.e., zero ‡uid velocity relative to the solid at the ‡uid-solid interface, has been very successful in describing many macroscopic ‡ows. A problem of principle arises when the no-slip boundary condition is used to model the hydrodynamics of immiscible-‡uid displacement in the vicinity of the moving contact line, where the interface separating two immiscible ‡uids intersects the solid wall. Decades ago it was already known that the moving contact line is incompatible with the no-slip boundary condition, since the latter would imply in…nite dissipation due to a non-integrable singularity in the stress near.In [8] Qian staded the contact-line motion in immiscible two-phase ‡ow, from molecular dynamics (MD) simulations to continuum hydrodynamics calculations. 6138 H. Kh. Abdullah Multiphase ‡ows form when two or more partially or not miscible ‡uids are brought in contact and subjected to a pressure gradient. The resulting ‡ows display a rich phase behavior, e.g. as suspended droplets, bubbles, slugs or thin …lms. The ‡ow behavior is dependent on the relative ‡ow rates of the ‡uid phases involved, the resulting interaction between gravitational, interfacial, inertial and viscous forces and the wetting behavior of the channel walls.The alternating succession of immiscible ‡uid segments will play a particularly important role.Multiphase microchemical systems generally take advantage of the large interfacial areas, rapid mixing and reduced mass transfer limitations to achieve improved performance relative to conventional bench-scale systems (see [14].[15], [16].[17]) .Multiphase ‡ows provide several mechanisms for enhancing and extending the performance of single-phase micro‡uidic systems. The long di¤usion times and broad dispersion bands associated with singlephase pressure-driven ‡ow can be reduced by adding a second, immiscible, ‡uid stream. . Examples of gas–liquid reactions that were performed in microreactors include direct ‡uorination( [18],[19]). Dynamic contact line phenomena involve two immiscible viscous ‡uids in contact with a solid surface; as one of the ‡uids displaces the other, the contact line moves along the solid surface. Applications range from droplet spreading in various applications to coating ‡ows. Such ‡ows have been studied both theoretically and experimentally (see [2], [6]). Simulating such ‡ows is complicated by the mathematical paradox of a contact line moving along a no-slip solid surface. Analytical solutions of the Navier–Stokes equations lead to a stress singularity at the contact line (see [4],[6]). This non-physical divergent stress stems from the fact that continuum ‡uid mechanics breaks down at molecular distances from the contact line; to circumvent the stress singularity, the molecular interactions between the ‡uids and the solid would have to be modeled.The standard model for two-phase ‡ow consists of the incompressible Navier–Stokes equations, combined with a mechanism to transport the interface with the local ‡uid velocity. This model cannot be combined with conventional no-slip boundary conditions at solids because this would lead to a singularity in the stresses around the contact line (see [10]). The singularity in the model can be avoided if the contact line is allowed to slip (see [11]).The Navier condition is su¢ cient for ‡ows that are driven by external forces. For capillary-driven ‡ows, on the other hand, the contact angle between the interface and the solid must also be taken into account. In numerical algorithms based on the level set method [12] or the volume of ‡uid method [13]. We consider a vertical rivulet of liquid with density, and viscosity ( 1 , 1 ) in a second ‡uid with density, and viscosity ( 2 , 2 ), where 1 > 2 , the latter being at rest at a large distance from the rivulet. In practical case of water rivulet in air, we should expect the small ratio of the viscosity’s to ensure that the motion of the air has little e¤ect on the ‡ow in the rivulet. But there are many cases of ‡uid ‡ow in which, as some parameters ( her the viscosity ratio) On two immiscible ‡uids 6139 tends to zero. The solution of the limiting form of the governing equations is di¤erent from the limiting form of the solution of the full equations. The objective of this paper is to answer the question: “ Dose the outer ‡uid has an important e¤ect on the rivulet?”, and how dose it e¤ect on the stability of the interface between the two ‡ows? We will obtain the explicit solution of the conventional governing equations of ‡uid near contact line. 2. Flow Description and Governing Equations. A vertical rivulet of liquid with density, and viscosity ( 1 , 1 ) in a second ‡uid with density, and viscosity ( 2 , 2 ) where 1 > 2 , the latter being at rest a large distance from the rivulet which is ‡ow steadily in the negative direction of the Z axis. Thus, if U1 ,V1 ; W and U2 ,V2 ; W2 are the velocity components of the ‡uids then,U1 = U2 = V1 = V2 = 0; W1 = W1 (X; Y ), and W2 = W2 (X; Y ): The partisan of the solid boundary between AB (see …g-1-) is in contact with the …rst ‡uid, the partisan above A and lowerB being in contact with the second ‡uid. The interface between the two ‡uids is characterized by a uniform surface tension , and by a contact angle , between the solid boundary and the tangent line to S at A, and B. We adopt a plane polar coordinate system (r, ). The speci…cation of the coordinate system is completed by taking the ray = 0, and = to be the tangent lines to S atB and A respectively. The Navier - Stokes equations inside and outside the rivulet becomes: . @P1 (2.1) 0 = 1g + 1 r2 w1 (r; ) @Z (2.2) (2.3) 0= 2g @P2 + @Z 2r 2 w2 (r; ) @P1 @P2 = =0 @ @ @P1 @P2 = =0 @r @r whereP1 ; P2 the pressures , are both independent of r; . The outer boundary w2 =) 0 , as r =) 1 , then gives (2.4) @P2 = 2g @Z the pressure di¤erence P across the rivulet is independent of Z, and this is because of the normal stress condition from the Laplace’s condition (2.5) (2.6) ( P )s = R H. Kh. Abdullah 6140 where R is the local radius of curvature of S, is the surface tension of the liquid. Since the interface S is a circular cylinder, and the pressure di¤erence P across it is independent of Z, we must have @P1 @P2 = = 2g @Z @Z Using (2.5), and (2.6) in (2.1), and (2.2) we get. (2.7) r2 w1 (r; ) = (2.8) where k = ( 1 2 1 k; )g r2 w2 (r; ) = 0: The boundary conditions are: a- The slip condition on AB (2.9) w1 (r; 0) = w2 (r; 0) , for all values of r (2.10) w1 (r; ) = w2 (r; ); for all values of r b- The shear stress condition (2.11) w1 (r; ) = w2 (r; ); (2.12) 1( @w1 )s = @r 2( @w2 )s @r 3. Local Theory Near a Contact Line Now we will try to answer the question: Does the outer ‡uid has an important e¤ect on the rivulet? To answer this question , …rst we assume that the ambient gas has no signi…cant e¤ect. The equation of motion with the boundary conditions from (2.8).(2.10), and (2.11) will be (3.1) r2 w1 (r; ) = k1 ; where k1 = 1g , 1 and (3.2) w1 (r; ) = 0; at = 0, for all values of r , On two immiscible ‡uids 6141 @w1 = 0; at = , for all values of r: @ Using separation of variable to homogeneous form of (3.1) (i.e. to r2 w1 (r; ) = 0 ) by seeking the solution of the form w1 (r; ) = R(r) ( ) , we get (3.3) 00 r2 R00 rR0 + = = R R where eigenvalues. To …nd the solution w1 for (3.1) we have two cases: case 1: If = 2 , let w1 (r; ) = r2 2 ( ) be the solution of (3.1) with the boundary conditions (3,2), by substituting, we get (3.4) 00 (3.5) ( )+4 ( )= k1 ; and (3.6) (0) = 0 ( ) = 0: The general solution of (3.1) will be (3.7) provided that k1 (cos 2 + tan 2 4 and 6= 34 : w1 (r; ) = r2 6= 4 sin 2 1); H. Kh. Abdullah 6142 case 2: if 6= 2; let (3.8) X ( ) be the solution of (3.1) then, r w1 (r; ) = 1 X bn r ( 12 +n) 2 n=1 Now the solution of (3.1) will be I- for > 4 , then 2 < 2, and n = 0, w1 = b0 r( 2 ) sin II- for > 3 4 w1 = b0 r( 2 ) sin then 2 3 2 0 1 sin(( + ) : 2 2 = , then 2 k1 (cos 2 + tan 2 sin 2 2 4 < 2, and n = 1, 1 = 23 , then + r2 3 +b1 r( 2 ) sin 3 2 +r2 1) k1 (cos 2 + tan 2 4 sin 2 1) III- for < 4 , 2 > 2 , n = 0 , 0 = 2 then the solution will be as in (I) above. IV- for < 4 , 2 > 2 , n = 1 , 1 = 23 then the solution will be as in (II) above. Now for = 4 , or = 34 , let the solution of (3.1) be of the form w1 = r2 ln r f ( ) + r2 g( ) substituting in (3.1) we will get the following di¤erential equations with boundary conditions (3.9) f 00 ( ) + 4f ( ) = 0; With the boundary conditions (3.10) f 0 ( ) + 4f ( ) = 0 and (3.11) g 0 ( ) + 4g( ) = 4f (0) k1 With the boundary conditions (3.12) g(0) = g 0 ( ) = 0: The solution of (3.9) is f (0) = A sin 2 , where A is constant and the solution of (3.11) is (3.13) g( ) = B sin 2 + k1 [( 4 ) cos 2 ]: Where B is arbitrary constant. Then, from (3.12) and (3.13) we get A = 4k1 ;thus f (0) = the solution w1 (r; ) of (3.1) will take the form k1 4 sin 2 , then On two immiscible ‡uids w1 (r; ) = (3.14) For = 4 k1 2 k1 2 r ln r(sin 2 ) + r [( 4 4 1 X 1 1 + bn r( 2 +n) sin +n 2 n=1 ; n = 0 and 0 = 4 6143 ] + Br2 sin 2 ) cos 2 : ; the solution will be of the form (3.15) k1 2 k1 2 r (sin 2 ) + r [( ) cos 2 ] + Br2 sin 2 + b0 r2 sin 2 : 4 4 = 34 ; n = 1 and 1 = 23 ; the solution will be of the form w1 (r; ) = For w1 (r; ) = (3.16) k1 2 k1 2 r (sin 2 ) + r [( 4 4 +b1 r2 sin 2 ] + Br2 sin 2 + b0 r2 sin 2 ) cos 2 4. Two Immiscible Fluids in Contact With Each Other on a Vertical Plane For the equations (2.6) and (2.9), let the solution be of the form w1 (r; ) = r 1 ( ); and w2 (r; ) = r 2 ( ); where is the eigenvalues to be found and is of two cases I- if = 2 then the solution will be (4.1) w1 (r; ) = k1 2 r (sin 2 4 sin 2 cos 2 1); and (4.2) II- if (4.3) w2 (r; ) = k1 2 r 1 8 1 2 sin 2 (1 cos 2 ) sin 2 : 2 1 6= 2;using the boundary condition (2.9) we get tan( )= c tan 2 ; where (4.4) w1 (r; ) = Br sin 1 cos2 c where B is arbitrary constant and c = ferent cases: (4.5) w2 (r; ) = Br (sin2 + : ) (sin 2 1 1 2 tan cos 2 ) ; the parameter c has three dif- 6144 H. Kh. Abdullah i - if c = 0 then = 2 : ii - if c =) 0 then = : iii - if c =) 1 then = 2( ) : These cases are shown in …g-2-. 5. Conclusion from …g-2- we conclude that the dominate solution will be in the interval < < 32 , and the point ( 2 ; 1) is a node point , ( 3 ; 23 ) is a saddle point . It means that the the system reaches stability at ( 2 ; 1). For the range < 3 the system is unstable and this range of is the range of most previous work. Now as 2 =) 0; then equation (4.1) will be exactly the same form as (3.7), 1 and as 2 =) 0; the de…nition or r in the two formulas become identical. these 1 results therefore con…rm the negligible e¤ect of the ambient atmosphere. 1 2 Acknowledgement 1. I would like to extend my thanks to the University of Sharjah for its support. On two immiscible ‡uids 6145 References 1.Ablett, (1923). An Investigation of the Angle of Contact Between Para¢ n Wax and Water., Phil. Mag., Vol. 46, PP 244-256 2.Billingham J. , On a model for the motion of a contact line on a smooth solid surface,(2006), European Journal of Applied Mathematics, vol.17, PP 347–382. 3.Culkin, J.B. , & Davis, S.H. (1981). Meandering of Water Rivulets. J. Amer. Inst. Chem. Engr., Vol. 30, PP 263-267. 4. Dussan V, E.B., and Davis S.H., On the motion of a ‡uid–‡uid interface along a solid surface (1974), Journal of Fluid Mechanics, vol.65, PP 71–95. 5.Dussan V., E. B. On the Spreading of Liquid on Solid Surface-Static And Dynamic Contact Lines (1979), Annual Review of Fluid Mech., Vol. 11, PP 3721-400. 6. Huh C., and Scriven L.E., Hydrodynamic model of steady movement of a solid/liquid/‡uid contact line (1971), Journal of Colloid and Interface Science, vol. 35, No.1, PP 85–101. 7.Young, G.W., & Davis, S.H.(1987) Rivulet Instabilities., J. of Fluid Mech., Vol. 176, PP 1-31. 8. Qian1 T., Wang X. P. and Sheng P.; Molecular Hydrodynamics of the Moving Contact Line in Two-Phase Immiscible Flows (2006), Commun. Comput. Phys., Vol.1, No.1PP 1-52. 9. Afkhami S., Zaleski S., and Bussmann M.,A mesh-dependent model for applying dynamic contact angles to VOF simulations (2009), Journal of Computational Physics, vol. 228, PP 5370 –5389. 10. Moriarty J.A.,and Schwartz L.W., E¤ective slip in numerical calculations of moving-contact-line problems (1992), Journal of Engineering Mathematics, vol. 26,81–86. 11. Š. Šikalo, Wilhelm H.D., Roisman I.V., Jakirli S., and Tropea C., Dynamic contact angle of spreading droplets: experiments and simulations(2005), Physics of Fluids, vol. 17, No.6, PP 062103. 12.Popinet S.,and Gerris: a tree-based adaptive solver for the incompressible Euler equations in complex geometries (2003), Journal of Computational Physics, vol.190, No.2, PP 572-600. 13. Renardy M., Renardy Y.,and Li J., Numerical simulation of moving contact line problems using a volume-of-‡uid method (200 1), Journal of Computational Physics, vol.171, No.1, PP 243-263. 14. Hessel V., Angeli P., Gavriilidis A., and Lowe H., Gas–liquid and gas– liquid–solid microstructured reactors: contacting principles and applications (2005),Industrial and Engineering Chemistry Research,vol.44, PP 9750–9769. 15. Jensen K.F., Microreaction engineering -is small better(2001)? Chemical Engineering Science, vol.56, PP 293–303. 6146 H. Kh. Abdullah 16. Hatakeyama T., Chen D.L.L., and Ismagilov R.F., Microgram-scale testing of reaction conditions in solution using nanoliter plugs in micro‡uidics with detection by MALDI-MS(2006), Journal of theAmerican Chemical Society, vol.128, PP 2518–2519. 17. Zheng B., and IsmagilovR.F., A micro‡uidic approach for screening submicroliter volumes against multiple reagents by using preformed arrays of nanoliter plugs in a three-phase liquid/liquid/gas ‡ow (20050, Angewandte Chemie International Edition, vol. 44, PP 2520–2523. 18. Chambers R.D., Fox M.A., Holling D., Nakano T., Okazoe, and Sandford G.,Elemental ‡uorine – Part 16, Versatile thin-…lm gas–liquid multi-channel microreactors for e¤ective scale-out(2005), Lab on a Chip, Vol.5, PP191–198. 19. Kawai K., Ebata T., Kitazume T., The synthesis of ‡uorinated materials in microreactors(2005), Journal of FluorineChemistry, vol.126, PP 956–961. Received: July, 2012
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