dean

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M4A33: Flow in curved pipes: the Dean equations Consider flow down a slowly curved pipe. In terms of cylindrical polar coordinates (r, φ, z ) we shall model this as a portion of a torus, (r - b) 2 + z 2 = a 2 where b a, and seek solutions independent of φ, driven by a pressure gradient in the φ-direction. The velocity u =(u r ,u φ ,u z ) satisfies the Navier Stokes equations 1 r ∂r (ru r )+ ∂u z ∂z =0 ρ Du r Dt - u 2 φ r = - p ∂r + μ 2 u r - u r r 2 ρ Du φ Dt + u φ u r r = G(r, z, t)+ μ 2 u φ - u φ r 2 ρ Du z Dt = - p ∂z + μ2 u z (1) where the material derivative D/Dt = ∂/∂t + u r ∂/∂r + u z ∂/∂z . Here G is the downpipe pressure gradient, G = -1/r ∂p/∂φ. We shall seek steady solutions to these equations. Let us first see if there is a unidirectional solution, as for the straight pipe. If we substitute u r =0= u z , we find p ∂z =0 and p ∂r = u 2 φ r = ∂u φ ∂z =0 . (2) So such a solution is only possible if u φ is constant on cylinders. Such a flow would be consistent with a no-slip condition only for flows between concentric cylinders. Any curved pipe-flow cannot be unidirectional. However, if the pipe is almost straight, we might expect the flow to be almost unidi- rectional. Now r and z vary over the scale a and we assume b a so that r = b + ax * b and ∂r 1 a 1 r (3) We scale z = az * and let U 0 be a typical scale of u φ . Then we expect a suitable scale for the pressure to be p ρU 2 0 a/b and if we scale u r ∂u r ∂r u z ∂u r ∂z u 2 φ r = u r u z U 0 a b 1 2 . (4) We therefore write u φ = U 0 u * φ u r,z = U 0 a b 1 2 u * x,z p = ρU 2 0 a b p * (5) 1

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Effect of dean parameter on flow field

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  • M4A33: Flow in curved pipes: the Dean equations

    Consider flow down a slowly curved pipe. In terms of cylindrical polar coordinates(r, , z) we shall model this as a portion of a torus, (r b)2 + z2 = a2 where b a, andseek solutions independent of , driven by a pressure gradient in the -direction.

    The velocity u = (ur, u, uz) satisfies the Navier Stokes equations

    1

    r

    r(rur) +

    uz

    z= 0

    (Dur

    Dtu2

    r

    )

    = p

    r+

    (2ur

    ur

    r2

    )

    (Du

    Dt+uur

    r

    )

    = G(r, z, t) + (2u

    u

    r2

    )

    Duz

    Dt=

    p

    z+ 2uz

    (1)

    where the material derivative D/Dt = /t+ ur/r + uz/z. Here G is the downpipepressure gradient, G = 1/r p/. We shall seek steady solutions to these equations.Let us first see if there is a unidirectional solution, as for the straight pipe. If we substituteur = 0 = uz, we find

    p

    z= 0 and

    p

    r=u2r

    =u

    z= 0 . (2)

    So such a solution is only possible if u is constant on cylinders. Such a flow would beconsistent with a no-slip condition only for flows between concentric cylinders. Any curvedpipe-flow cannot be unidirectional.

    However, if the pipe is almost straight, we might expect the flow to be almost unidi-rectional. Now r and z vary over the scale a and we assume

    b a so that r = b+ ax ' b and

    r

    1

    a

    1

    r(3)

    We scale z = az and let U0 be a typical scale of u. Then we expect a suitable scale forthe pressure to be p U20 a/b and if we scale

    urur

    r uz

    ur

    zu2r

    = ur uz U0(ab

    ) 12. (4)

    We therefore write

    u = U0u ur,z = U0

    (ab

    ) 12ux,z p = U

    20

    (ab

    )p (5)

    1

  • and neglecting terms of order (a/b), equations (1) become

    uxx

    +uzz

    = 0

    U20b

    (DuxDtu21

    )

    = U20b

    p

    x+U0

    a2

    (ab

    )12 2ux

    U20(ab)1/2

    DuDt

    = G+U0

    a22u

    U20b

    (DuzDt

    )

    =U20b

    p

    z+U0

    a2

    (ab

    ) 12 2uz

    (6)

    We choose the scale U0 and define a parameter K such that

    Ga2

    U0= 1 and K =

    U0a

    (ab

    )12. (7)

    From now on we drop the from all the dimensionless variables to obtain the Deanequations.

    ux

    x+uz

    z= 0

    K

    (Dux

    Dt u2

    )

    = Kp

    x+2ux

    KDu

    Dt= 1 +2u

    KDuz

    Dt= K

    p

    z+2uz

    . (8)

    These equations are essentially the two-dimensional Navier-Stokes equations with a bodyforce u2 acting towards the inside of the bend. If we write u = (u, v, w) in Cartesiancoordinates (x, y, z), and introduce a stream function, (x, z) where u ux = /zand w uz = /x, and v(x, z) u, then (8) reduce to

    K(zvx xvz) = 1 +2v

    K(zx xz) = 2 2Kvvz

    }

    (9)

    where = 2 is the downpipe vorticity and suffices now denote partial derivatives.These equations are to be solved for v(x, z) and (x, z) subject to the no-slip conditions

    = 0, v = 0 on the pipe boundary. (10)

    There is one parameter in the problem, K, which is known as the Dean number and definedin (7). It is a Reynolds number modified by the pipe curvature, (a/b).

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