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Fluid Mechanics Test 3

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Fluid Mechanics Test 3
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  • Question 1
    1 / -0
    A two- dimensional flow field is defined as \(\vec V = \vec ix - \vec jy\) the equation of the streamline passing through the point (1, 2) is 
    Solution

    Concept:

    Streamline: It is the line along which stream function ψ remains constant.

    If ψ = f (x,y)

    dψ = 0

    \(d\psi = \frac{{\partial \psi }}{{\partial x}}dx + \frac{{\partial \psi }}{{\partial y}}dy\)

    For streamline dψ = 0

    \(\begin{array}{l} vdx - udy = 0\\ \therefore \frac{{dx}}{u} = \frac{{dy}}{v} \end{array}\)

    Calculation:

    Given, \(\vec V = \vec ix - \vec jy\)

    So, u = x and v = -y

    Streamline equation: \(\frac{{dx}}{u} = \frac{{dy}}{v}\)

    \(\frac{{dx}}{x} = \frac{{dy}}{{ - y}}\)

    Integrating both side

    ln x = -ln y + ln c

    xy = c

    Given x =1 , y =2

    so, c =2

    so equation is xy – 2 = 0

  • Question 2
    1 / -0

    Find the value of ‘a’ for fluid flow given by V = (axy2 + 2y)î + (3xy + x2y)ĵ.

    It is given that flow is steady incompressible flow at (1, 1).
    Solution

    Concept:

    Continuity equation should be satisfied for incompressible, steady flow,

    \(\frac{{\partial u}}{{\partial x}} + \frac{{\partial v}}{{\partial y}} = 0\)

    Calculation:

    \(\frac{\partial }{{\partial x}}\left( {ax{y^2} + 2y} \right) + \frac{\partial }{{\partial y}}\left( {3xy + {x^2}y} \right) = 0\)

    (ay2) + (3x + x2) = 0

    At (1, 1)

    a + (3 + 1) = 0

    ∴ a = - 4
  • Question 3
    1 / -0
    Find the flow rate across two points P (4, 2) an Q (1, 1), given that stream function Ψ = 3x(y2 + 1) + 2x3 _______
    Solution

    Concept:

    Flow rate between two points P & Q = ΨP – ΨQ

    Calculation:

    ΨP = 3(4)(4 + 1) + 2(4)3 = 188

    ΨQ = 3(1 + 1) + 2(1) = 8

    ΨP – ΨQ = 188 – 8

    ∴ ΨP – ΨQ = 180
  • Question 4
    1 / -0
    The circulation ‘Γ’ around a circle of radius 2 units for the velocity field u = 2x + 3y and v = - 2y is
    Solution

    Concept:

    Circulation = Vorticity × Area

    where, 

    Vorticity is defined as the value twice of the rotation.

    ζ = 2ω

    Rotation (ω) =  \({\omega _z} = \frac{1}{2}\left( {\frac{{\partial v}}{{\partial x}} - \frac{{\partial u}}{{\partial y}}} \right)\)

    Now,

    ∴ Vorticity = \(\zeta = \frac{{\partial v}}{{\partial x}} - \frac{{\partial u}}{{\partial y}} \)

    Calculation:

    Circulation = Vorticity × Area

    \(Circulation= \left( {\frac{{\partial v}}{{\partial x}} - \frac{{\partial u}}{{\partial y}}} \right) \times Area\)

    Circulation= (0 – 3) × π × (2)2

    ∴ Circulation= -12π units

  • Question 5
    1 / -0

    In a two-dimensional incompressible steady flow, the velocity component u = Aex is obtained. What is the other component ‘v’ of velocity?

    Solution

    Concept:

    For incompressible steady flow, Laplace equation must be satisfied

    \(\begin{array}{l} \frac{{{d^2}\phi }}{{d{x^2}}} + \frac{{{d^2}\phi }}{{d{y^2}}} = 0\\ \frac{{d\phi }}{{dx}} = - u = - A{e^x} \Rightarrow \frac{{{d^2}\phi }}{{d{x^2}}} = - A{e^x}\\ - A{e^x} + \frac{{{d^2}\phi }}{{d{y^2}}} = 0\\ \therefore \frac{{{d^2}\phi }}{{d{y^2}}} = A{e^x}\\ V = - \frac{{d\phi }}{{dy}} = A{e^x}y + f\left( x \right) \end{array}\)

    -V = Aex.y + f(x)

    ∴ V = -Aex.y + f(x)

  • Question 6
    1 / -0

    A leaf is caught in a whirlpool. At a given instant, the leaf is at a distance of 120 m from the centre of the whirlpool. The whirlpool can be described by the following velocity distribution:

    \({V_r} = - \left( {\frac{{60 \times {{10}^3}}}{{2\pi r}}} \right)\frac{m}{s}\;and\;{V_\theta } = \frac{{300 \times {{10}^3}}}{{2\pi r}}m/s\;\)where r (in meters) is the distance from the centre of the whirlpool. What will be the distance of the leaf from the centre when it has moved through half a revolution?

    Solution

    Explanation:

    Given: 

    The leaf is at a distance of 120 m from the center of the whirlpool.

    To calculate = distance of the leaf from the center when it has moved through half a revolution

    Now,

    \(\begin{array}{l} \frac{{{V_\theta }}}{{{V_r}}} = - \left( {\frac{{300 \times {{10}^3}}}{{2\pi r}}} \right) \times \frac{{2\pi r}}{{\left( {60 \times {{10}^3}} \right)}} = - 5\\ \Rightarrow \frac{{{V_r}}}{{{V_\theta }}} = - \frac{1}{5} \Rightarrow {V_r} = - \frac{{{V_\theta }}}{5}\\ \Rightarrow {V_r} = \frac{{dr}}{{dt}}\;and\;{V_\theta } = r\frac{{d\theta }}{{dt}}\;\\ \Rightarrow \frac{{dr}}{{dt}} = - \frac{r}{5}\frac{{d\theta }}{{dt}} \Rightarrow \frac{{dr}}{r} = - \frac{{d\theta }}{5}\\ \mathop \smallint \limits_{120}^r \frac{{dr}}{r} = - \frac{1}{5}\mathop \smallint \limits_0^\pi d\theta \\ \Rightarrow \left| {\ln r} \right|_{120}^r = - \frac{\pi }{5}\\ \Rightarrow \ln \frac{r}{{120}} = - \frac{\pi }{5}\\ \Rightarrow \frac{r}{{120}} = {e^{ - \pi /5}} \end{array}\)

    ∴ r = 64 m

  • Question 7
    1 / -0
    Water is directed vertically upwards from a nozzle of 20 m diameter with a velocity of 10 m/s. What will be the diameter of water jet at a point 3 m above the nozzle? Assume the jet remains circular and neglected only loss of energy.
    Solution

    Concept:

    Equation used: V2 = u2 + 2gh

    Continuity equation : A1V1 = A2V2

    Calculation:

    Given: D = 20 mm = 0.02 m, u = 10 m/s, h = 3 m

    Now,

    V2 = u2 + 2gh

    V2 = 102 + 2 (-9.81) (3) [ Velocity of jet at height (h) = 3 m]

    V2 = 41.14

    V = 6.414 m/s

    Now, applying continuity equation

    A1V1 = A2V2

    \(\frac{\pi }{4}\left( {{D^2}} \right)\left( {10} \right) = \frac{\pi }{4}{d^2}\left( {6.414} \right)\)

    d = 0.02497 m

    ∴ d = 24.97 mm
  • Question 8
    1 / -0

    Find convective acceleration at point P(2, 1) for the given stream function

    Ψ = 2x2y
    Solution

    Concept:

    \({\rm{Total\;acceleration\;}}\left( a \right) = \sqrt {a_x^2 + a_y^2} \)

    \({a_x} = u \cdot \frac{{\partial u}}{{\partial x}} + v \cdot \frac{{\partial u}}{{\partial y}}\)

    \({a_y} = u \cdot \frac{{\partial v}}{{\partial x}} + v \cdot \frac{{\partial v}}{{\partial y}}\)

    \({\rm{Also}},{\rm{\;}}u = \frac{{ - \partial \psi }}{{dy}}\;\;;\;\;v = \frac{{\partial \psi }}{{\partial x}}\)

    Calculation:

    Ψ = 2x2y         (Given)

    \(u = \frac{{ - \partial }}{{dy}}\left( {2{x^2}y} \right) = - 2{x^2} = - 2\left( {{2^2}} \right) = - 8\)

    \(v = \frac{\partial }{{\partial x}}\left( {2{x^2}y} \right) = 4xy = 4\left( 2 \right) = 8\)

    \({a_x} = \left( { - 8} \right)\;\frac{\partial }{{\partial x}}\left( { - 2{x^2}} \right) + 8 \cdot \frac{\partial }{{\partial y}}\left( { - 2{x^2}} \right)\;\)

    ax = (-8)(-4x) + 0 = 32x = 64

    \({a_y} = \left( { - 8} \right)\frac{\partial }{{\partial x}}\left( {4xy} \right) + \left( 8 \right)\frac{\partial }{{\partial y}}\left( {4xy} \right)\;\)

    a= (-8)(4y) + 8(4x)

    ay = -32 + 64 = 32

    Now,

    \({\rm{Total\;acceleration\;}}\left( a \right) = \sqrt {a_x^2 + a_y^2} \)

    \({\rm{Total\;acceleration\;}}\left( {\rm{a}} \right) = \sqrt {{{64}^2} + {{32}^2}} \)

    ∴ Total acceleration (a) = 71.55
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