Engineering Hydraulics II
CEC3190            Prof. Talib Mansoor
                            Unit 1
Open channel flow and its classifications,
Channel properties,
Basic   Principles:   continuity,    energy   and   momentum
principles,
Critical flow computation and its applications,
Transitions with sub critical and super critical flows.
                                    Unit 2
   Uniform flow,
   roughness coefficient,
   computation of uniform flow in prismatic channel,
   design of non- erodible channels for uniform flow,
   Most efficient channel section,
   Compound sections.
                                    Unit 3
Gradually varied flow: Theory and analysis,
gradually-varied flow computations in prismatic channels,
gradually varied flow in non-prismatic channels.
Rapidly varied flow: Theory of hydraulic jump,
evaluation of jump elements in rectangular and non-rectangular channel,
location of jump on horizontal floor,
channel controls and transitions,
free over fall, thin plate weirs, broad crested weirs, and sluice gates
                          Unit 4
Application of model studies to free surface flow problems,
waves and their classifications,
celerity of a wave,
surge formation,
equation of motion,
rapidly varied unsteady flows.
  Text Books and/or Reference Materials
  1. Subramanya, “Flow in Open channels”
  2. K G Ranga Raju, “Flow through open channel”
  3. V.T chow “Open channel Hydraulics”
  4. Bakhmeteff, “Hydraulics of open channel”
  5. Henderson, “Open Channel Flow”
             DIFFERENCE BETWEEN PIPE & CHANNEL FLOW
             PIPE FLOW                            CHANNEL FLOW
 Pipe has finite shape, size or cross    Channel may or may not have finite
   section                                  shape, size or cross section
 Pipe has same roughness throughout      Channel may or may not have the
                                            same roughness throughout
 Flow is under pressure or               Flow is under gravity and
   pressurized flow                         characterized by free surface
 Velocity is maximum at the axis and     Velocity is maximum near the free
   velocity distribution is parabolic       surface and velocity distribution is
                                            logarithmic
                                 Types of channels
                  1. Natural channel and Artificial channel
Various types of artificial channels:
• A canal is a long channel having mild slope excavated in ground.
• A flume is the channel made of wood, metal, concrete or masonry usually
  supported on or above ground.
• A chute is a channel having steep slope and almost vertical sides.
• A drop is similar to chute but the change in the bed elevation is effected in
  a short distance.
• A culvert is a short channel flowing partly full.
      PRISMATIC AND NON-PRISMATIC CHANNELS
     PRISMATIC CHANNELS: A channel in which the cross sectional shape, size
      and the bottom slope are constant is termed as prismatic channel. Most of the
      man-made channel are prismatic channels over long stretches. The rectangular,
      trapezoidal, triangular and circular are commonly used shapes in manmade
      channels.
     NON-PRISMATIC CHANNELS: All natural channels like rivers drains etc.
      generally have varying cross section and consequently are non-prismatic.
   RIGID AND MOBILE BOUNDARY CHANNELS
 RIGID BOUNDARY CHANNELS: Rigid channels are those in which the
  boundary is not deformable. The shape and roughness magnitudes are not
  functions of flow parameters. For example, lined canals and non-erodible
  unlined canals.
 In Rigid channels the flow velocity and shear stress distribution will be such that
  no major scouring, erosion or deposition will take place in the channel and the
  channel geometry and roughness are essentially constant with respect to time.
  MOBILE BOUNDARY CHANNELS: When the boundary of the channel is
    mobile and flow carries considerable amounts of sediment through suspension
    and is in contact with the bed. Such channels are classified as mobile channels.
  In the mobile channel, not only depth of flow but also bed width, longitudinal
    slope of channel may undergo changes with space and time depending on type
    of flow.
  The resistance to flow, quantity of sediment transported and channel geometry
    all depends on interaction of flow with channel boundaries.
                           Types of open channel flow
         Based on Reynold’s number: Ratio of inertial force to viscous force is
          known as Reynold’s number (Re)
                 𝑉𝐿
         𝑅𝑒 =
                 𝜈
         V= characteristic velocity generally taken as average velocity over the entire
          cross section, L= characteristic length (Hydraulic Radius R= A/P)
                 𝑉𝑅
         𝑅𝑒 =
                  𝜈
         If    Re ≤ 500            Laminar flow
         If    500 ≤ Re ≤ 2000     Transition
         And         Re ≥ 2000     Turbulent flow
                                Based on Froude number
 Ratio of inertial force to gravity force is known as Froude number (F)
        𝑉
𝐹 =           L= characteristic length generally taken as hydraulic depth (D=A/T) in
        𝑔𝐿
  open channel
        𝑉
𝐹 =
        𝑔𝐷
F<1           subcritical flow
F=1           critical flow
F>1           supercritical flow or rapid flow or shooting flow
FOUR REGIMES
Subcritical laminar:        F < 1 Re ≤ 500
Supercritical laminar:      F < 1 Re ≤ 500
Subcritical turbulent:      F < 1 Re ≥ 2000
Supercritical turbulent:    F > 1 Re ≥ 2000
In most of the cases flow in open channel is subcritical turbulent.
        Based on space & time:
        1-D flow:            V= f (x, t)
        2-D flow:            V= f (x, y, t)
        3-D flow:            V= f (x, y, z, t)
                                Space dependent
 Uniform & Non uniform flow: If flow property like flow velocity, flow
    depth remains constant along the channel length at an instant, the flow is said
    to be uniform. Convective acceleration is zero in uniform flow.
     𝜕𝑉          𝜕𝑦
           =0          =0
     𝜕𝑥 𝑡        𝜕𝑥 𝑡
 A flow in which flow properties changes with channel length is termed as
    Non uniform flow (Varied flow). Convective acceleration exists in non-
    uniform flow.
                                Time dependent
 Steady & Unsteady Flow: If flow property like flow velocity, flow depth
    remains constant with time at a section, the flow is said to be steady. Local
    acceleration is zero in steady flow.
     𝜕𝑉           𝜕𝑦
           =0           =0
     𝜕𝑡 𝑥         𝜕𝑡 𝑥
 If flow property like flow velocity, flow depth changes with time at a section,
    the flow is termed as unsteady. Local acceleration exists in unsteady flow.
                                      Channel properties
          Four shapes are widely used for carrying water through open
          channels
           Rectangular
           Triangular
           Trapezoidal
           Circular
              Area         Top Width     Wetted        Hydraulic         Hydraulic           Section
Section                                Perimeter         Radius             Depth            Factor
               (A)            (T)          (P)          (R=A/P)           (D=A/T)          (Z=A 𝑫)
               By             B           B+2y             𝐵𝑦                  y              𝐵𝑦 3/2
                                                         𝐵 + 2𝑦
              𝑚𝑦 2           2my       2𝑦 1 + 𝑚2           𝑚𝑦                  𝑦              2𝑚𝑦 5/2
                                                                               2
                                                       2 1 + 𝑚2
            y(B+my)         B+2my      𝐵 + 2𝑦 1 + 𝑚2
                                                         𝑦(𝐵 + 𝑚𝑦)       𝑦(𝐵 + 𝑚𝑦)         𝑦 𝐵 + 𝑚𝑦       1.5
                                                       𝐵 + 2𝑦   1 + 𝑚2                         𝐵 + 2𝑚𝑦
                                                                          𝐵 + 2𝑚𝑦
          𝐷02               𝐷0 𝑆𝑖𝑛𝜃        𝐷0 𝜃        𝐷0 2𝜃 − 𝑆𝑖𝑛2𝜃     𝐷0 2𝜃 − 𝑆𝑖𝑛2𝜃   𝐷02.5 (2𝜃 − 𝑆𝑖𝑛2𝜃)1.5
              2𝜃 − 𝑆𝑖𝑛2𝜃
          8                                                  8𝜃              8𝑆𝑖𝑛𝜃             512𝑆𝑖𝑛2𝜃
Velocity Distribution in Open Channel
  Engineering Hydraulics II
                CEC3190
               Lecture – 2
                                 Prof. Talib Mansoor
Velocity Distribution in open channel
                     Field observations in rivers and canals
                      show that average velocity vav at any
                      vertical occurs at 0.6y0 from free surface
                      where y0 is the flow depth.
                              𝑣0.2 +𝑣0.8
                     𝑣𝑎𝑣 =
                                   2
                     This equation is generally employed
                      while stream gauging to determine
                      discharge using area velocity method.
                     𝑣𝑎𝑣 = 𝑘𝑣𝑠
                     Where 𝑣𝑠 is surface velocity,
                     k varies from 0.8 to 0.9 depending upon the
                    channel section
1-D method of flow analysis
                             If v is the velocity associated
                              with a small area dA at any
                              cross section, then average
                              velocity at that section can be
                              determined by
                                       1
                             𝑉 = 𝐴𝑑𝑣 
                                 𝐴
                             𝑄 = 𝑉𝐴 = 𝐴𝑑𝑣 
Kinetic Energy Correction Factor
          Mass flow rate through a small area dA at section xx = ρvdA
                                               1
          Energy flow rate through this area = 𝜌𝑣𝑑𝐴𝑣 2
                                               2
          Energy flux passing through entire cross sectional area
             1
          =  𝑣𝐴𝑑𝜌 3            (1)
             2
          If V is the average velocity at the section under consideration and
          A is the entire cross sectional area, then
          Energy flux passing through entire cross sectional area
              1
          = 𝛼 𝜌𝐴𝑉 3             (2)
              2
          Where α is kinetic energy correction factor. From (1) and (2)
                𝑣 3 𝑑𝐴
          𝛼=                    (3)
                  𝑉 3𝐴
          Value of α is greater than unity. For straight prismatic channel its
          value is 1.10
Momentum Correction Factor
             Mass flow rate through a small area dA at section xx= ρvdA
             Momentum flow rate through this area = 𝜌𝑣𝑑𝐴𝑣
             Momentum flux passing through entire cross sectional area
             =  𝑣𝐴𝑑𝜌 2         (1)
             If V is the average velocity at the section under
             consideration and A is the entire cross sectional area, then
             Energy flux passing through entire cross sectional area
             = 𝛽𝜌𝐴𝑉 2           (2)
             Where α is kinetic energy correction factor. From (1) and (2)
                      𝑣 2 𝑑𝐴
             𝛽=                 (3)
                         𝑉 2𝐴
             Value of 𝛽 is greater than unity. For straight prismatic
             channel its value is 1.05
                  Basic Principles
         Continuity Equation for steady state flow
                        Assumptions
                        • No flow is entering or leaving the channel
                          boundaries
                        • Fluid is incompressible
                        • Rate of mass inflow through area dA1 at section 1
                        = ρv1dA1        (1)
                        Rate of mass outflow through area dA2 at section 2
                        = ρv2dA2        (2)
Equating (1) and (2)
ρv1dA1 = ρv2dA2
integrating both sides to obtain total mass inflow at
section1 and 2
𝑣𝜌 1 𝑑𝐴1 = 𝑣𝜌 2 𝑑𝐴2
𝑉1 𝐴1 = 𝑉2 𝐴2
Where V1 and V2 are the average velocities and A1 and A2
are the areas at section 1 and 2 respectively.
      Continuity Equation for Unsteady flow ( Q2 > Q1 )
                                        gate is closed at the upstream
                                                         𝜕𝑄
                                        ΔQ = Q2 – Q1 =        ∆𝑥
                                                         𝜕𝑥
                                        In time Δt excess volume of outflow
                                                    𝜕𝑄
                                        = ΔQ Δt =        ∆𝑥 ∆𝑡     (1)
                                                    𝜕𝑥
                                        In time Δt decrease in storage volume
                                                         𝜕𝐴
                                        = -ΔA Δx = −          ∆𝑡 ∆𝑥      (2)
                                                         𝜕𝑡
Equating (1) and (2)
 𝜕𝑄                     𝜕𝐴
         ∆𝑥 ∆𝑡 = −           ∆𝑡 ∆𝑥
 𝜕𝑥                     𝜕𝑡
 𝜕𝑄           𝜕𝐴
          +            =0         (3)
 𝜕𝑥           𝜕𝑡
Since TΔy = ΔA, dividing both sides by Δt
    ∆𝑦       ∆𝐴
𝑇        =
    ∆𝑡       ∆𝑡
    𝜕𝑦       𝜕𝐴
𝑇        =        substituting in (3)
    𝜕𝑡       𝜕𝑡
𝜕𝑄           𝜕𝑦
     +𝑇           =0              (4)
𝜕𝑥           𝜕𝑡
Same equation is valid for Q1 > Q2, that will produce rise in depth and (1)
and (2) will be replaced by outflow volume (-) and increase in storage
volume (+).
     Euler’s equation of motion: 𝑭𝒑 + 𝑭𝒈 = 𝒎𝒂𝒔
                                                Pressure at face 1 = p
                                                                           𝜕𝑝
                                                Pressure at face 2 = 𝑝 +      ∆𝑠
                                                                           𝜕𝑠
                                                Force on face 1, F1 = p.Δn.1
                                                                             𝜕𝑝
                                                Force on face 2, F2 = (p +      ∆𝑠)Δn.1
                                                                             𝜕𝑠
                                                Weight of fluid element dW = γΔsΔn.1
                                                Its component along s direction = dWsinθ
                                                                    𝜕𝑧
                                                        = −𝛾∆𝑠∆𝑛         downward slope
                                                                    𝜕𝑠
σ 𝐹 = 𝑚𝑎𝑠
𝐹1 − 𝐹2 + 𝑑𝑊𝑠𝑖𝑛𝜃 = 𝑚𝑎𝑠
                    𝜕𝑝                           𝜕𝑧
𝑝∆𝑛 − 𝑝 +              ∆𝑠    ∆𝑛 − 𝛾∆𝑠∆𝑛               = 𝜌∆𝑠∆𝑛𝑎𝑠
                    𝜕𝑠                           𝜕𝑠
     𝜕𝑝        𝜕𝑧            𝜕𝑉𝑠          𝜕𝑉𝑠
 −        −𝛾           =𝜌          + 𝑉𝑠
     𝜕𝑠        𝜕𝑠            𝜕𝑡           𝜕𝑠
    𝜕𝑉𝑠          𝜕𝑉𝑠        𝜕
𝜌         + 𝑉𝑠         +         𝑝 + 𝛾𝑧 = 0                       (1)
    𝜕𝑡           𝜕𝑠         𝜕𝑠
This equation is Euler’s equation of motion
      Unsteady Non uniform flow:
      Multiplying (1) by ds and integrating
            𝜕𝑉𝑠
      𝜌        𝑑𝑠   + 𝜌  𝑠𝑑 𝑠𝑉 +  𝑝(𝑑 + 𝛾𝑧) = 𝑐𝑜𝑛𝑠𝑡𝑡
            𝜕𝑡
      Dividing by γ
      1 𝜕𝑉𝑠              𝑉𝑠2    𝑝
      𝑔
        𝑠𝑑 𝑡𝜕       +
                         2𝑔
                               + +𝑧 =0
                                𝛾
      Since variation of Vs with t is not known, this equation is
      not useful for general analysis,
Steady Non uniform flow
𝜕𝑉𝑠
      =0
𝜕𝑡
Equation (1) is modified as
      𝜕𝑉𝑠       𝜕
𝜌𝑉𝑠         +        𝑝 + 𝛾𝑧 = 0
      𝜕𝑠        𝜕𝑠
Multiplying by ds, dividing by γ and integrating
𝑉𝑠2    𝑝
      + + 𝑧 = 𝑐𝑜𝑛𝑠𝑡𝑡                Bernoulli’s equation
2𝑔     𝛾
Steady uniform flow
𝜕𝑉𝑠                 𝜕𝑉𝑠
      = 0, and 𝑉𝑠         =0
𝜕𝑡                  𝜕𝑠
Equation (1) can be written as
𝜕
      𝑝 + 𝛾𝑧 = 0
𝜕𝑠
Integration yields
𝑝 + 𝛾𝑧 = 0
𝑝
    +𝑧 =0
𝛾
Piezometric head or hydrostatic pressure distribution.
    Momentum equation
                                     Assumptions
                                      Steady flow
                                      Incompressible fluid
                                      Prismatic channel
                                      No lateral inflow or outflow
consider control volume between section 1 and 2
Hydrostatic force at section 1 F1 = γ A1 ̅y1
Hydrostatic force at section 2 F2 = γ A2 ̅y2
Component of weight acting in x direction = Wsinθ
Frictional force acting on the sides and bed of the channel = Ff = τ0PL
Where τ0 is average shear stress acting on bed and sides of the channel
Equation of motion
σ 𝐹 = rate of change of momentum = ρQ(𝛽2V2 - 𝛽1V1)
γ A1 ̅y1 - γ A2 ̅y2 + Wsinθ - τ0PL = ρQ(𝛽2V2 - 𝛽1V1)              (1)
 Specific Force (F)
 Equation (1) can be modified with the following
 assumptions
 Channel bed is horizontal, boundary frictionless and
 momentum correction factor is unity
                                              1     1
 γ A1 y̅ 1 - γ A2 y̅ 2 = ρQ(V2 - V1) = 𝜌𝑄 2   𝐴2
                                                   −𝐴       (2)
                                                        1
                       𝑄2   1         1
 A1 y̅ 1 - A2 y̅ 2 =   𝑔    𝐴2
                                 −𝐴
                                       1
             𝑄2                  𝑄2
 A1 y̅ 1 +         = A2 y̅ 2 +
             𝑔𝐴1                 𝑔𝐴2
                  𝑄2
 F = A y̅ + 𝑔𝐴                                              (3)
Specific Force (F)
Equation (1) can be modified with the following assumptions
Channel bed is horizontal, boundary frictionless and momentum correction factor is unity
                                           1        1
γ A1 ̅y1 - γ A2 ̅y2 = ρQ(V2 - V1) = 𝜌𝑄 2        −         (2)
                                           𝐴2       𝐴1
                     𝑄2   1         1
A1 ̅y1 - A2 ̅y2 =              −
                     𝑔    𝐴2       𝐴1
           𝑄2                  𝑄2
A1 ̅y1 +         = A2 ̅y2 +
           𝑔𝐴1                 𝑔𝐴2
                𝑄2
F = A ̅y +                                                (3)
                𝑔𝐴
Force per unit specific weight
                               Engineering Hydraulics II
                                                CEC3190
                                           Lecture – 3
                                                              Prof. Talib Mansoor
                                           Specific Energy
                                                Bekhmeteff (1912) introduced the concept
                                                of specific energy. The total energy at any
                                                section of an open channel carrying flow
                                                at depth y with velocity V is given by
                                                                         𝑉2
                                                𝐻 = 𝑧 + 𝑦𝐶𝑜𝑠𝜃 + 𝛼
                                                                         2𝑔
                                                If the channel bottom is assumed as datum
                                                (Z=0), the total energy (H) is reduced to
                                                specific energy (E).
                                                                    𝑉2
                                                𝐸 = 𝑦𝐶𝑜𝑠𝜃 + 𝛼
                                                                    2𝑔
If the channel bottom is assumed as datum (Z=0), the total energy (H) is reduced to
           specific energy (E).
                 𝑉2
𝐸 = 𝑦𝐶𝑜𝑠𝜃 + 𝛼
                 2𝑔
For channel of small bed slope θ ≈ 0, assuming uniform velocity distribution α =1
         𝑉2
𝐸 =𝑦+           For steady state flow V =Q/A
         2𝑔
          𝑄2
𝐸 =𝑦+                   (1) A=f(y)          E=f(y)      Eq (1) represents a Cubic Parabola.
         2𝑔𝐴2
Solution of (1) for given values of E and Q yields three roots for y i. e. y1, y2 and y3.
        y1 +ve (larger) corresponds to subcritical flow
        y2 +ve (smaller) corresponds to supercritical flow and
        y3 -ve (meaningless and ignored)
                                       For channel of small bed slope
                                       θ ≈ 0, assuming uniform velocity
                                       distribution α =1
                                                  𝑉2
                                       𝐸 =𝑦+
                                                  2𝑔
                                                   𝑄2
                                       𝐸 =𝑦+               (1)
                                                  2𝑔𝐴2
                              Critical Flow
When flow is critical
 Froude Number is unity
 Specific Energy is minimum for a given discharge
 Discharge is maximum for given specific energy
 Specific Force is minimum for a given discharge
 Discharge is maximum for given specific force
          𝑄2
𝐸 =𝑦+                   (1)
         2𝑔𝐴2
            1. Specific energy is minimum for given discharge at critical flow
            For E to be minimum, differentiate (1) w r t y and equate it to zero
   𝑑𝐸                𝑄2 −2 𝑑𝐴              𝑄2 𝑇
        =1+                          =1−          =0
   𝑑𝑦                2𝑔 𝐴3 𝑑𝑦              𝑔𝐴3
            𝑄2 𝑇
                   =1
            𝑔𝐴3
            𝑉2𝑇
                   =1
            𝑔𝐴
             𝑉2
                     =1
            𝑔𝐴/𝑇
            𝑉2
                 =1
            𝑔𝐷
             𝑉
                   =1
             𝑔𝐷
            𝐹=1
2. Discharge is maximum for a given specific energy at critical flow
Rearranging (1)
𝑄 = 𝐴 2𝑔(𝐸 − 𝑦)                      (2)
   For Q to be maximum, differentiate (2) w r t y and equate it to zero
   𝑑𝑄                       1                          𝑑𝐴
        =          2𝑔 𝐴              0−1 + 𝐸−𝑦              =0
   𝑑𝑦                     2 𝐸−𝑦                        𝑑𝑦
        𝐴                       𝑑𝐴
                 =    𝐸−𝑦
   2 𝐸−𝑦                        𝑑𝑦
   𝐴
       = 𝐸−𝑦 𝑇
   2
   Substituting the value of (E-y) form (2)
   𝐴         𝑄2 𝑇
       =
   2         2𝑔𝐴2
   𝑄2 𝑇
            =1
   𝑔𝐴3
   𝐹=1
               3. Specific force is minimum for given discharge at critical flow
                                                        𝑄2
                                         𝐹 = 𝐴𝑦ത +                  (3)
                                                        𝑔𝐴
                                         For a given Q, A = f(y) and F = f(y)
                                         For F to be minimum, differentiate (3) w r t y and
                                         equate it to zero
                                                   𝑑𝐹   𝑑       𝑄2 −1 𝑑𝐴
                                                      =   𝐴𝑦ത +
                                                   𝑑𝑦 𝑑𝑦        𝑔 𝐴2 𝑑𝑦
                                              𝑑              𝑄2 𝑇
                                         =       (𝐴𝑦)
                                                   ത    −           =0
                                              𝑑𝑦             𝑔𝐴2
                                         𝑑              𝑄2 𝑇
                                               𝐴𝑦ത =                      (4)
                                         𝑑𝑦             𝑔𝐴2
                                         𝐴𝑦ത = moment of area about free surface
Change in moment of area due to small change in depth can be computed as below
      Taking moment of area about top free surface -2
                                          ∆𝑦                                    ∆𝑦
𝐴𝑦ത + ∆ 𝐴𝑦ത = 𝐴 𝑦ത + ∆𝑦 + ∆𝐴 ×               =    𝐴 𝑦ത + ∆𝑦 + 𝑇∆𝑦 ×
                                           2                                     2
                                         (∆𝑦)2
𝐴𝑦ത + ∆ 𝐴𝑦ത = 𝐴 𝑦ത + ∆𝑦 + 𝑇 ×
                                           2
Neglecting second term
∆ 𝐴𝑦ത = 𝐴∆𝑦
∆ 𝐴𝑦ത
         =𝐴
 ∆𝑦
Within limits ∆𝑦 → 0
𝑑 𝐴𝑦ത
         =𝐴         (5)     Substituting in (4)
 𝑑𝑦
        𝑄2 𝑇         𝑄2 𝑇
𝐴=                          =1      𝐹=1
        𝑔𝐴2          𝑔𝐴3
4. Discharge is maximum for given Specific force at critical flow
              𝑄2
 𝐹 = 𝐴𝑦ത +              (3)
              𝑔𝐴
 Rearranging (3)
 𝑄=     𝑔𝐴(𝐹 − 𝐴𝑦)
                ത                 (4)
 For Q to be maximum, differentiate (4) w r t y and equate it to zero
 𝑑𝑄           1 𝑑𝐴                         𝐴           𝑑
      = 𝑔                 𝐹 − 𝐴𝑦ത +               0−        𝐴𝑦ത   =0
 𝑑𝑦          2 𝐴 𝑑𝑦                     2 𝐹−𝐴𝑦ത        𝑑𝑦
 Using (5)
   1 𝑑𝐴                       𝐴
             𝐹 − 𝐴𝑦ത +                  0−𝐴       =0
  2 𝐴 𝑑𝑦                   2 𝐹−𝐴𝑦ത
            Rearranging the terms
            𝑇 𝐹 − 𝐴𝑦ത = 𝐴2                     using (3)
            𝑄2 𝑇
                   = 𝐴2
            𝑔𝐴
            𝑄2 𝑇
                   =1
            𝑔𝐴3
            𝐹=1
                             Critical flow computations (yc and Ec)
Rectangular channel
A = By
                                                                 Specific energy
T=B
                                                                            𝑄2           𝐴3𝑐
                                                                 𝐸𝑐 = 𝑦𝑐 +       = 𝑦𝑐 +
At critical flow                                                           2𝑔𝐴2𝑐        2𝑇𝑐 𝐴2𝑐
               𝑄2 𝐴3𝑐 𝐵3 𝑦𝑐3
                 =    =      = 𝐵2 𝑦𝑐3                                     𝐴𝑐
               𝑔   𝑇𝑐   𝐵                                        = 𝑦𝑐 +
                                                                          2𝑇𝑐
𝑄2                                        𝑞2
       = 𝑦𝑐3                                   = 𝑦𝑐3                        𝐵𝑦𝑐     3
𝐵2 𝑔                                      𝑔                     𝐸𝑐 = 𝑦𝑐 +         = 𝑦𝑐 = 1.5𝑦𝑐
                                                                            2𝐵      2
Critical depth of flow
                          𝑞2
                                      1/3                       𝐸𝑐 = 1.5𝑦𝑐
                     𝑦𝑐 =
                          𝑔
                             Triangular channel
        A = my2
        T = 2my
        At critical flow
        𝑄2         𝐴3𝑐       𝑚3 𝑦𝑐6       𝑚2 𝑦𝑐5
               =         =            =                Specific energy
        𝑔          𝑇𝑐        2𝑚𝑦𝑐          2
        𝑦𝑐5 =
                   2𝑄2                                           𝐴𝑐         𝑚𝑦𝑐2        𝑦𝑐
                   𝑔𝑚2                                 𝐸𝑐 = 𝑦𝑐 +     = 𝑦𝑐 +      = 𝑦𝑐 +
                                                                 2𝑇𝑐        4𝑚𝑦𝑐        4
                                                         5
        Critical depth of flow                         = 𝑦𝑐
                                                         4
                              1/5
                    2𝑄2
        𝑦𝑐 =                                           𝐸𝑐 = 1.25𝑦𝑐
                    𝑔𝑚2
                               Trapezoidal channel
A = y(B+my)
T = B+2my
At critical flow
𝑄2       𝐴3𝑐       𝑦𝑐3 𝐵+𝑚𝑦𝑐 3
     =         =                     (1)
𝑔        𝑇𝑐           𝐵+2𝑚𝑦𝑐
yc can be computed by trial & error. Non-dimensional form of (1) facilitate the solution
of yc with the help of graphs and tables. Taking B common from Numerator &
denominator and making depth dimensionless by denoting
                   𝑚𝑦𝑐
          𝜁𝑐 =
                    𝐵
          𝑄2        𝐵2 𝑦𝑐3 1+𝑚𝜁𝑐 3
               =
          𝑔             1+2𝑚𝜁𝑐
                      𝑄2       𝐵5 𝜁𝑐3 1+𝑚𝜁𝑐 3
                           =
                      𝑔         𝑚3 1+2𝑚𝜁𝑐
                      𝑄 2 𝑚3       𝜁𝑐3 1+𝑚𝜁𝑐 3
                               =
                       𝑔𝐵5            1+2𝑚𝜁𝑐
                                            3/2
                      𝑄𝑚3/2                𝜁𝑐     1+𝑚𝜁𝑐 3/2
                                =𝜓=
                       𝑔𝐵5/2                    1+2𝑚𝜁𝑐 1/2
                      For given Q ,m and B, 𝜁𝑐 and hence yc can be determined
                      A plot between 𝜓 and , 𝜁𝑐 can be prepared to calculate yc
                      Table 2A-2 gives values of 𝜓 and , 𝜁𝑐 (Subramanya)
                               Circular channel
         𝐷02
𝐴=              2𝜃 − 𝑆𝑖𝑛2𝜃
          8
𝑇 = 𝐷0 𝜃
At critical flow
𝑄2       𝐴3𝑐       𝐷06 2𝜃𝑐 −𝑆𝑖𝑛2𝜃𝑐 3
     =         =
𝑔        𝑇𝑐           512𝐷0 𝑆𝑖𝑛𝜃𝑐
 𝑄2            2𝜃𝑐 −𝑆𝑖𝑛2𝜃𝑐 3
         =
𝑔𝐷05            512𝑆𝑖𝑛𝜃𝑐
     𝑄           0.044194 2𝜃𝑐 −𝑆𝑖𝑛2𝜃𝑐 3/2              𝑦
   5/2       =                                     = 𝑓( 𝑐 )
 𝑔𝐷0                    (𝑆𝑖𝑛𝜃𝑐 )1/2                    𝐷0
                    Section factor
                                             1/2
                                        𝐴3
                    Z=A 𝐷 =
                                        𝑇
                      2        𝐴3       𝑄2
                    𝑍 =             =
                               𝑇        𝑔
                               𝑄2
                    𝑍𝑐2   =
                               𝑔
                        𝑄            𝑍𝑐              𝑦
                        5/2     =    5/2     = 𝑓( 𝑐 )
                      𝑔𝐷0           𝐷0               𝐷0
                                               𝑦𝑐           𝑍𝑐
                    From table find                  for    5/2   and then yc
                                               𝐷0          𝐷0
                                CHANNEL TRANSITIONS
may be defined as the change in the channel cross section. This may be provided by changing
the bed elevation (step rise or step fall) or by altering the channel bed width (contraction or
expansion). Such a geometric change may be gradual or sudden. Generally, transitions are
designed for minimum or no loss.
Engineering Hydraulics II
       CEC3190
      Lecture – 5
                Prof. Talib Mansoor
Engineering Hydraulics II
       CEC3190
      Lecture – 6
                Prof. Talib Mansoor
Write the four cases
             SOLVE THESE TWO PARTS
b). If the bed is raised by 10cm, what should be channel
bed width at section 2 to produce critical flow there.
c). If the bed is raised by 10cm and width is reduced to
3.4m, determine the flow depths y1 and y2.
Engineering Hydraulics II
       CEC3190
      Lecture – 7
                  Prof. Talib Mansoor
             Reduction in width
             with hump
Problem: Water is flowing in 4 m wide rectangular channel at the rate of 20
m3/s with depth 2m. At a particular section downstream channel width is
reduced to 3.8m. Assuming no loss in transition
a. determine flow depths y1 and y2 if the bed at section 2 is raised by 12cm,
b. Determine bed elevation ΔZ to produce critical flow at section 2.
c. determine flow depths y1 and y2 if the bed at section 2 is raised by 25cm