Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering PDF Download

Mechanisms of Boundary Layer Transition

  • One of the interesting problems in fluid mechanics is the physical mechanism of transition from laminar to turbulent flow. The problem evolves about the generation of both steady and unsteady vorticity near a body, its subsequent molecular diffusion, its kinematic and dynamic convection and redistribution downstream, and the resulting feedback on the velocity and pressure fields near the body. We can perhaps realise the complexity of the transition problem by examining the behaviour of a real flow past a cylinder. 

    Fig.31.4 (a) shows the flow past a cylinder for a very low Reynolds number Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering . The flow smoothly divides and reunites around the cylinder. 

  • At a Reynolds number of about 4, the flow (boundary layer) separates in the downstream and the wake is formed by two symmetric eddies . The eddies remain steady and symmetrical but grow in size up to a Reynolds number of about 40 as shown in Fig.31.4 (b)
  • At a Reynolds number above 40 oscillation in the wake induces asymmetry and finally the wake starts shedding vortices into the stream. This situation is termed as onset of periodicity as shown inFig.31.4 (c) and the wake keeps on undulating up to a Reynolds number of 90 
  • At a Reynolds number above 90 , the eddies are shed alternately from a top and bottom of the cylinder and the regular pattern of alternately shed clockwise and counterclockwise vortices form Von Karman vortex street as in Fig.31.4 (d).
  • Periodicity is eventually induced in the flow field with the vortex-shedding phenomenon. 
     
  • The periodicity is characterised by the frequency of vortex shedding f 
  • In non-dimensional form, the vortex shedding frequency is expressed as Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering  known as theStrouhal number named after V. Strouhal, a German physicist who experimented with wires singing in the wind. The Strouhal number shows a slight but continuous variation with Reynolds number around a value of 0.21. The boundary layer on the cylinder surface remains laminar and separation takes placeat about 81from the forward stagnation point. 
  • At about Re = 500 , multiple frequencies start showing up and the wake tends to become Chaotic. 
     
  • As the Reynolds number becomes higher, the boundary layer around the cylinder tends to become turbulent. The wake, of course, shows fully turbulent characters (Fig.31.4 (e) ).
  • For larger Reynolds numbers, the boundary layer becomes turbulent. A turbulent boundary layer offers greater resistance to seperation than a laminar boundary layer. As a consequence the seperation point moves downstream and the seperation angle is delayed to 1100 from the forward stagnation point (Fig.31.4 (f) ).

 

Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering
Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering
Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering
Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering

  • Experimental flow visualizations past a circular cylinder are shown in Figure 31.5 (a) and (b)

Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering

Fig 31.5 (a) Flow Past a Cylinder at Re=2000 [Photograph courtesy Werle and Gallon (ONERA)]


Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering
Fig 31.5 (b) Flow Past a Cylinder at Re=10000 [Photograph courtesy
 Thomas Corke and Hasan Najib (Illinois Institute of Technology, Chicago)]

 

 

  • A very interesting sequence of events begins to develop when the Reynolds number is increased beyond 40, at which point the wake behind the cylinder becomes unstable. Photographs show that the wake develops a slow oscillation in which the velocity is periodic in time and downstream distance. The amplitude of the oscillation increases downstream. The oscillating wake rolls up into two staggered rows of vortices with opposite sense of rotation.
     
  • Karman investigated the phenomenon and concluded that a nonstaggered row of vortices is unstable, and a staggered row is stable only if the ratio of lateral distance between the vortices to their longitudinal distance is 0.28. Because of the similarity of the wake with footprints in a street, the staggered row of vortices behind a blue body is called a Karman Vortex Street . The vortices move downstream at a speed smaller than the upstream velocity U
     
  • In the range 40 < Re < 80, the vortex street does not interact with the pair of attached vortices. As Re is increased beyond 80 the vortex street forms closer to the cylinder, and the attached eddies themselves begin to oscillate. Finally the attached eddies periodically break off alternately from the two sides of the cylinder.
     
  • While an eddy on one side is shed, that on the other side forms, resulting in an unsteady flow near the cylinder. As vortices of opposite circulations are shed off alternately from the two sides, the circulation around the cylinder changes sign, resulting in an oscillating "lift" or lateral force. If the frequency of vortex shedding is close to the natural frequency of some mode of vibration of the cylinder body, then an appreciable lateral vibration culminates. 
     
  • Numerical flow visualizations for the flow past a circular cylinder can be observed in Fig 31.6 and 31.7
  • An understanding of the transitional flow processes will help in practical problems either by improving procedures for predicting positions or for determining methods of advancing or retarding the transition position.
  • The critical value at which the transition occurs in pipe flow is Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering . The actual value depends upon the disturbance in flow. Some experiments have shown the critical Reynolds number to reach as high as 10,000. The precise upper bound is not known, but the lower bound appears to be Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical EngineeringBelow this value, the flow remains laminar even when subjected to strong disturbances.
  • In the case of flow through a channel,  Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering, the flow alternates randomly between laminar and partially turbulent. Near the centerline, the flow is more laminar than turbulent, whereas near the wall, the flow is more turbulent than laminar. For flow over a flat plate, turbulent regime is observed between Reynolds numbers  Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering  of 3.5 × 105 and 106.

 

Several Events Of Transition -

Transitional flow consists of several events as shown in Fig. 31.8. Let us consider the events one after another.


1. Region of instability of small wavy disturbances-  

Consider a laminar flow over a flat plate aligned with the flow direction (Fig. 31.8).

  • In the presence of an adverse pressure gradient, at a high Reynolds number (water velocity approximately 9-cm/sec), two-dimensional waves appear.
  • These waves are called Tollmien-Schlichting wave( In 1929, Tollmien and Schlichting predicted that the waves would form and grow in the boundary layer).
  •  These waves can be made visible by a method known as tellurium method. 

2. Three-dimensional waves and vortex formation-

  • Disturbances in the free stream or oscillations in the upstream boundary layer can generate wave growth, which has a variation in the span wise direction.
  • This leads an initially two-dimensional wave to a three-dimensional form.
  • In many such transitional flows, periodicity is observed in the span wise direction. 
  • This is accompanied by the appearance of vortices whose axes lie in the direction of flow.

3. Peak-Valley development with streamwise vortices-

  • As the three-dimensional wave propagates downstream, the boundary layer flow develops into a complex stream wise vortex system.
  • Within this vortex system, at some spanwise location, the velocities fluctuate violently 
  • These locations are called peaks and the neighbouring locations of the peaks are valleys (Fig. 31.9).

4. Vorticity concentration and shear layer development-
    
At the spanwise locations corresponding to the peak, the instantaneous streamwise velocity profiles demonstrate the following

  •  Often, an inflexion is observed on the velocity profile.
  •  The inflectional profile appears and disappears once after each cycle of the basic wave.

5. Breakdown-
  
  
The instantaneous velocity profiles produce high shear in the outer region of the boundary layer.

  • The velocity fluctuations develop from the shear layer at a higher frequency than that of the basic wave.
  • These velocity fluctuations have a strong ability to amplify any slight three-dimensionality, which is already present in the flow field.
  • As a result, a staggered vortex pattern evolves with the streamwise wavelength twice the wavelength of Tollmien-Schlichting wavelength .
  • The span wise wavelength of these structures is about one-half of the stream wise value. 
  • The high frequency fluctuations are referred as hairpin eddies.

This is known as breakdown. 

6. Turbulent-spot development-

  • The hairpin-eddies travel at a speed grater than that of the basic (primary) waves. 
  • As they travel downstream, eddies spread in the spanwise direction and towards the wall.
  • The vortices begin a cascading breakdown into smaller vortices.
  • In such a fluctuating state, intense local changes occur at random locations in the shear layer near the wall in the form of turbulent spots.
  • Each spot grows almost linearly with the downstream distance.

  The creation of spots is considered as the main event of transition . 

Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering

Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering

The document Entry Flow in a Duct - 2 | Fluid Mechanics for Mechanical Engineering is a part of the Mechanical Engineering Course Fluid Mechanics for Mechanical Engineering.
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FAQs on Entry Flow in a Duct - 2 - Fluid Mechanics for Mechanical Engineering

1. What is the purpose of an entry flow in a duct?
Ans. The purpose of an entry flow in a duct is to ensure smooth and efficient airflow into the duct system. It helps to minimize pressure losses, turbulence, and energy wastage by controlling the direction and velocity of the incoming air.
2. How does the entry flow affect the performance of a duct system?
Ans. The entry flow plays a crucial role in determining the overall performance of a duct system. If the entry flow is well-designed and optimized, it can minimize pressure drops, improve energy efficiency, and reduce noise levels. Conversely, a poorly designed entry flow can lead to increased turbulence, higher pressure losses, and decreased system performance.
3. What factors should be considered when designing an entry flow in a duct?
Ans. Several factors need to be considered when designing an entry flow in a duct. These include the duct geometry, inlet shape, velocity profile, and the desired airflow rate. Additionally, factors such as the duct material, environmental conditions, and any specific requirements or constraints should also be taken into account during the design process.
4. Can the entry flow in a duct be optimized for different types of fluids?
Ans. Yes, the entry flow in a duct can be optimized for different types of fluids. The design considerations may vary depending on the specific characteristics of the fluid, such as viscosity and density. By taking into account the fluid properties and applying appropriate design principles, the entry flow can be tailored to ensure efficient flow for a wide range of fluids.
5. Are there any specific guidelines or standards available for designing entry flows in duct systems?
Ans. Yes, there are specific guidelines and standards available for designing entry flows in duct systems. Organizations such as the American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE) provide guidelines and standards that outline best practices for duct design, including the design of entry flows. These guidelines can help ensure that the entry flow is optimized for efficient and effective airflow in duct systems.
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