Outline
                              Introduction
                      Continuity Equation
                    Navier-Stokes Equation




                Basic Equations of Fluid Mechanics

                              Dr.-Ing. Naseem Uddin

                          Mechanical Engineering Department
                       NED University of Engineering & Technology




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction
                      Continuity Equation
                    Navier-Stokes Equation




     1 Introduction

     2 Continuity Equation
           Differential formulation
           Integral formulation of Continuity Equation

     3 Navier-Stokes Equation
           Balance of forces
           Constitutive Relations of Stokes
           Differential formulation
           Integral formulation of momentum equations

     Chapter 5(RTT) and 6 Munson etal.


Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction
                      Continuity Equation
                    Navier-Stokes Equation


Basic laws of Physics



                  1 Law of conservation of mass ⇒
                    Continuity Equation
                  2 Law of conservation of momentum ⇒
                    Navier-Stokes Equation
                  3 Law of conservation of energy ⇒
                    Energy Equation




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction   Differential formulation
                      Continuity Equation    Integral formulation of Continuity Equation
                    Navier-Stokes Equation




        Mass cannot be created or
        destroyed. This laws for an
        infinitesimal control volume
        or region is called
        Continuity equation.
        Figure shows the mass
        balance for a fixed volume
        element in 2-dimensions (x,y
        plane). Depth is unity.




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction   Differential formulation
                      Continuity Equation    Integral formulation of Continuity Equation
                    Navier-Stokes Equation




     Velocity in x direction −→ u = u(x,y,z,t)
     Velocity in y direction −→ v= v(x,y,z,t)
     Velocity in z direction −→ w= w(x,y,z,t)
     Density ρ = ρ (x,y,z,t)
     Size: dx & dy
     Mass flow rate (m)= velocity normal to surface × surface area
                       ˙
     mx /unit area= ρ .u
      ˙
     my /unit area= ρ .v
      ˙
     mz /unit area= ρ .w
      ˙




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction    Differential formulation
                      Continuity Equation     Integral formulation of Continuity Equation
                    Navier-Stokes Equation




     Net mass flow rate = rate of mass accumulation/decrease in CV
     . Using Taylor series (neglecting higher order terms) we have:
     Net mass out-flow rate =
                        1 ∂ρu              1 ∂ρu
                     ρu +     dx dy − ρu −       dx dy
                        2 ∂x               2 ∂x
                        1 ∂ρv              1 ∂ρv
                 + ρv +       dy dx − ρv −       dy dx                           (1)
                        2 ∂y               2 ∂y

     Mass decrease in CV =
                                          ∂ρ
                                      −      dxdy                                (2)
                                          ∂t



Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction     Differential formulation
                      Continuity Equation      Integral formulation of Continuity Equation
                    Navier-Stokes Equation




     Simplify and we get:

                              ∂ρ ∂(ρu) ∂(ρv)
                                 +    +      =0                                   (3)
                              ∂t   ∂x   ∂y
     For three dimensions:
                        ∂ρ ∂(ρu) ∂(ρv) ∂(ρw)
                           +    +     +      =0                                   (4)
                        ∂t   ∂x   ∂y    ∂z

                                      ∂ρ
                                         +    .v = 0                              (5)
                                      ∂t
     where
                                     v = ui + v j + wk


Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction   Differential formulation
                      Continuity Equation    Integral formulation of Continuity Equation
                    Navier-Stokes Equation


Reynolds Transport Theorem


        A system of fluid is passing
        through a flow field
        V(x,y,z,t). The streamlines
        are shown in figure and
        system takes a new position
        in time t+∆ t. An extensive
        sytem property N is
        changing in the system. η is
        N per unit mass.




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction    Differential formulation
                      Continuity Equation     Integral formulation of Continuity Equation
                    Navier-Stokes Equation



     Three distinct regions are:
     I - System at time t
     II- System passing
     III- System at time t+∆ t

            dN                       (NIII + NII )t+∆t − (NI + NII )t
                = Lim∆t→0                                                        (6)
             dt                                     ∆t


      dN                     [(NII )t+∆t − (NII )t ] + (NIII )t+∆t − (NI )t
          = Lim∆t→0
       dt                                          ∆t
                                                                                 (7)

                            [(NII )t+∆t − (NII )t ]        ∂
              Lim∆t→0                                  =              ηρdϑ       (8)
                                     ∆t                    ∂t    CV


Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction   Differential formulation
                      Continuity Equation    Integral formulation of Continuity Equation
                    Navier-Stokes Equation

     Net efflux rate=
                                      (NIII )t+∆t − (NI )t
                         Lim∆t→0                                                (9)
                                               ∆t
        The volume of fluid that
        swept out of area dA in time
        dt is:

             dϑ = V dt dA cos α

        or
                  dϑ = (V.dA)
        Efflux rate through control
        surface =

                       ηρV.dA         (10)
                  CS
Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline
                              Introduction          Differential formulation
                      Continuity Equation           Integral formulation of Continuity Equation
                    Navier-Stokes Equation




                       dN                               ∂
                           =              ηρV.dA +                 ηρdϑ              (11)
                        dt           CS                 ∂t    CV
     Now as η = N/mass we have η=1 (in case of mass).

                     dM                                      ∂
                         =m=
                          ˙                    ρV.dA +                  ρdϑ          (12)
                      dt                  CS                 ∂t    CV

     for incompressible flows:

                                     m=
                                     ˙              ρV.dA                            (13)
                                               CS




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline   Balance of forces
                              Introduction   Constitutive Relations of Stokes
                      Continuity Equation    Differential formulation
                    Navier-Stokes Equation   Integral formulation of momentum equations



          1 Body forces fb (gravitational, magnetic etc.)
          2 Surface forces fs (pressure, forces due to shear & normal
          stresses)


                                      F = m.a                                (14)

                                              Du
                                     F = m.                                  (15)
                                              Dt
                                                Du
                                     F = ρ.ϑ.                                (16)
                                                Dt
                                 F               Du
                                   = fb + fs = ρ                             (17)
                                 ϑ               Dt

Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline   Balance of forces
                              Introduction   Constitutive Relations of Stokes
                      Continuity Equation    Differential formulation
                    Navier-Stokes Equation   Integral formulation of momentum equations




        There are two types of
        stresses, Normal strsses (σ)
        and shear stresses (τ ).




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline   Balance of forces
                              Introduction   Constitutive Relations of Stokes
                      Continuity Equation    Differential formulation
                    Navier-Stokes Equation   Integral formulation of momentum equations


Forces due to surface stresses




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline   Balance of forces
                              Introduction   Constitutive Relations of Stokes
                      Continuity Equation    Differential formulation
                    Navier-Stokes Equation   Integral formulation of momentum equations


     Net force in x direction=
                             ∂(σxx )        ∂(τyx )
                                     dxdy +         dxdy                     (18)
                               ∂x             ∂y

                        Du         ∂(σxx ) ∂(τyx ) ∂(τzx )
                    ρ      = ρfx +        +       +                          (19)
                        Dt           ∂x      ∂y      ∂z
     for y direction:

                        Dv         ∂(σyy ) ∂(τxy ) ∂(τzy )
                    ρ      = ρfy +        +       +                          (20)
                        Dt           ∂y     ∂x      ∂z
     for z direction:
                        Dw         ∂(σzz ) ∂(τyz ) ∂(τxz )
                    ρ      = ρfz +        +       +                          (21)
                        Dt           ∂z     ∂y      ∂x

Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline   Balance of forces
                              Introduction   Constitutive Relations of Stokes
                      Continuity Equation    Differential formulation
                    Navier-Stokes Equation   Integral formulation of momentum equations


Relation between stresses and velocity gradients


               2         ∂u
  σxx =     λ − µ Θ + 2µ    +A                                 ∂v   ∂u
               3         ∂x                          τxy =        +
                                                               ∂x ∂y
               2         ∂v
  σyy =     λ − µ Θ + 2µ    +A                                 ∂w ∂u
               3         ∂y                          τxz =        +
                                                               ∂x   ∂z
               2         ∂w
  σzz =     λ − µ Θ + 2µ    +A                                 ∂w ∂v
               3         ∂z                          τyz =        +
                                                               ∂y   ∂z
                ∂u ∂v ∂w
          Θ=      +   +
                ∂x ∂y   ∂z


Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline   Balance of forces
                              Introduction   Constitutive Relations of Stokes
                      Continuity Equation    Differential formulation
                    Navier-Stokes Equation   Integral formulation of momentum equations

     For simple flows A= - thermodynamic pressure = - Pthermo
     Average pressure =
                                  1
                             P = − (σxx + σyy + σzz )                        (22)
                                  3
     It is related to thermodynamic pressure as:
                                P = −λΘ + Pthermo                            (23)
     For constant density flows Θ is zero!
                                       2        ∂u
                             σxx = −P − µΘ + 2µ
                                       3        ∂x
                                      2        ∂v
                            σyy = −P − µΘ + 2µ
                                      3        ∂y
                                      2        ∂w
                            σzz = −P − µΘ + 2µ
                                      3        ∂z
Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline   Balance of forces
                              Introduction   Constitutive Relations of Stokes
                      Continuity Equation    Differential formulation
                    Navier-Stokes Equation   Integral formulation of momentum equations


Navier-Stokes Equations


         Du   ∂u    ∂u    ∂u    ∂u    1 ∂P                      2
            =    +u    +v    +w    =−      +                        u + fx     (24)
         Dt   ∂t    ∂x    ∂y    ∂z    ρ ∂x


         Dv   ∂v    ∂v    ∂v    ∂v    1 ∂P                      2
            =    +u    +v    +w    =−      +                        v + fy     (25)
         Dt   ∂t    ∂x    ∂y    ∂z    ρ ∂y


       Dw   ∂w    ∂w    ∂w    ∂w    1 ∂P                            2
          =    +u    +v    +w    =−      +                              w + fz (26)
       Dt   ∂t    ∂x    ∂y    ∂z    ρ ∂z


Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics
Outline        Balance of forces
                              Introduction        Constitutive Relations of Stokes
                      Continuity Equation         Differential formulation
                    Navier-Stokes Equation        Integral formulation of momentum equations




                       dN                             ∂
                           =              ηρV.dA +              ηρdϑ              (27)
                        dt           CS               ∂t   CV
     Now as η = N/mass we have η=V (in case of momentum).


        dM omentum                                              ∂
                   = F orce =                     VρV.dA +                Vρdϑ (28)
            dt                               CS                 ∂t   CV




Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te
Basic Equations of Fluid Mechanics

Basiceqs3

  • 1.
    Outline Introduction Continuity Equation Navier-Stokes Equation Basic Equations of Fluid Mechanics Dr.-Ing. Naseem Uddin Mechanical Engineering Department NED University of Engineering & Technology Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 2.
    Outline Introduction Continuity Equation Navier-Stokes Equation 1 Introduction 2 Continuity Equation Differential formulation Integral formulation of Continuity Equation 3 Navier-Stokes Equation Balance of forces Constitutive Relations of Stokes Differential formulation Integral formulation of momentum equations Chapter 5(RTT) and 6 Munson etal. Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 3.
    Outline Introduction Continuity Equation Navier-Stokes Equation Basic laws of Physics 1 Law of conservation of mass ⇒ Continuity Equation 2 Law of conservation of momentum ⇒ Navier-Stokes Equation 3 Law of conservation of energy ⇒ Energy Equation Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 4.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation Mass cannot be created or destroyed. This laws for an infinitesimal control volume or region is called Continuity equation. Figure shows the mass balance for a fixed volume element in 2-dimensions (x,y plane). Depth is unity. Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 5.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation Velocity in x direction −→ u = u(x,y,z,t) Velocity in y direction −→ v= v(x,y,z,t) Velocity in z direction −→ w= w(x,y,z,t) Density ρ = ρ (x,y,z,t) Size: dx & dy Mass flow rate (m)= velocity normal to surface × surface area ˙ mx /unit area= ρ .u ˙ my /unit area= ρ .v ˙ mz /unit area= ρ .w ˙ Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 6.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation Net mass flow rate = rate of mass accumulation/decrease in CV . Using Taylor series (neglecting higher order terms) we have: Net mass out-flow rate = 1 ∂ρu 1 ∂ρu ρu + dx dy − ρu − dx dy 2 ∂x 2 ∂x 1 ∂ρv 1 ∂ρv + ρv + dy dx − ρv − dy dx (1) 2 ∂y 2 ∂y Mass decrease in CV = ∂ρ − dxdy (2) ∂t Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 7.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation Simplify and we get: ∂ρ ∂(ρu) ∂(ρv) + + =0 (3) ∂t ∂x ∂y For three dimensions: ∂ρ ∂(ρu) ∂(ρv) ∂(ρw) + + + =0 (4) ∂t ∂x ∂y ∂z ∂ρ + .v = 0 (5) ∂t where v = ui + v j + wk Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 8.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation Reynolds Transport Theorem A system of fluid is passing through a flow field V(x,y,z,t). The streamlines are shown in figure and system takes a new position in time t+∆ t. An extensive sytem property N is changing in the system. η is N per unit mass. Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 9.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation Three distinct regions are: I - System at time t II- System passing III- System at time t+∆ t dN (NIII + NII )t+∆t − (NI + NII )t = Lim∆t→0 (6) dt ∆t dN [(NII )t+∆t − (NII )t ] + (NIII )t+∆t − (NI )t = Lim∆t→0 dt ∆t (7) [(NII )t+∆t − (NII )t ] ∂ Lim∆t→0 = ηρdϑ (8) ∆t ∂t CV Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 10.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation Net efflux rate= (NIII )t+∆t − (NI )t Lim∆t→0 (9) ∆t The volume of fluid that swept out of area dA in time dt is: dϑ = V dt dA cos α or dϑ = (V.dA) Efflux rate through control surface = ηρV.dA (10) CS Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 11.
    Outline Introduction Differential formulation Continuity Equation Integral formulation of Continuity Equation Navier-Stokes Equation dN ∂ = ηρV.dA + ηρdϑ (11) dt CS ∂t CV Now as η = N/mass we have η=1 (in case of mass). dM ∂ =m= ˙ ρV.dA + ρdϑ (12) dt CS ∂t CV for incompressible flows: m= ˙ ρV.dA (13) CS Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 12.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations 1 Body forces fb (gravitational, magnetic etc.) 2 Surface forces fs (pressure, forces due to shear & normal stresses) F = m.a (14) Du F = m. (15) Dt Du F = ρ.ϑ. (16) Dt F Du = fb + fs = ρ (17) ϑ Dt Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 13.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations There are two types of stresses, Normal strsses (σ) and shear stresses (τ ). Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 14.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations Forces due to surface stresses Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 15.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations Net force in x direction= ∂(σxx ) ∂(τyx ) dxdy + dxdy (18) ∂x ∂y Du ∂(σxx ) ∂(τyx ) ∂(τzx ) ρ = ρfx + + + (19) Dt ∂x ∂y ∂z for y direction: Dv ∂(σyy ) ∂(τxy ) ∂(τzy ) ρ = ρfy + + + (20) Dt ∂y ∂x ∂z for z direction: Dw ∂(σzz ) ∂(τyz ) ∂(τxz ) ρ = ρfz + + + (21) Dt ∂z ∂y ∂x Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 16.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations Relation between stresses and velocity gradients 2 ∂u σxx = λ − µ Θ + 2µ +A ∂v ∂u 3 ∂x τxy = + ∂x ∂y 2 ∂v σyy = λ − µ Θ + 2µ +A ∂w ∂u 3 ∂y τxz = + ∂x ∂z 2 ∂w σzz = λ − µ Θ + 2µ +A ∂w ∂v 3 ∂z τyz = + ∂y ∂z ∂u ∂v ∂w Θ= + + ∂x ∂y ∂z Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 17.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations For simple flows A= - thermodynamic pressure = - Pthermo Average pressure = 1 P = − (σxx + σyy + σzz ) (22) 3 It is related to thermodynamic pressure as: P = −λΘ + Pthermo (23) For constant density flows Θ is zero! 2 ∂u σxx = −P − µΘ + 2µ 3 ∂x 2 ∂v σyy = −P − µΘ + 2µ 3 ∂y 2 ∂w σzz = −P − µΘ + 2µ 3 ∂z Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 18.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations Navier-Stokes Equations Du ∂u ∂u ∂u ∂u 1 ∂P 2 = +u +v +w =− + u + fx (24) Dt ∂t ∂x ∂y ∂z ρ ∂x Dv ∂v ∂v ∂v ∂v 1 ∂P 2 = +u +v +w =− + v + fy (25) Dt ∂t ∂x ∂y ∂z ρ ∂y Dw ∂w ∂w ∂w ∂w 1 ∂P 2 = +u +v +w =− + w + fz (26) Dt ∂t ∂x ∂y ∂z ρ ∂z Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics
  • 19.
    Outline Balance of forces Introduction Constitutive Relations of Stokes Continuity Equation Differential formulation Navier-Stokes Equation Integral formulation of momentum equations dN ∂ = ηρV.dA + ηρdϑ (27) dt CS ∂t CV Now as η = N/mass we have η=V (in case of momentum). dM omentum ∂ = F orce = VρV.dA + Vρdϑ (28) dt CS ∂t CV Dr.-Ing. Naseem UddinMechanical Engineering Department NED University of Engineering & Te Basic Equations of Fluid Mechanics