Stream Function and Velocity Potential)
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NPTEL – Mechanical – Principle of Fluid Dynamics Module 3 : Lecture 1 INVISCID INCOMPRESSIBLE FLOW (Fundamental Aspects) In general, fluids have a well-known tendency to move or flow. The slight change in shear stress or appropriate imbalance in normal stresses will cause fluid motion. Fluid kinematics deals with various aspects of fluid motion without concerning the actual force that causes the fluid motion. In this particular section, we shall consider the ‘field’ concept to define velocity/ acceleration of fluid by virtue of its motion. In the later part, some ‘visualization’ concepts are introduced to define the motion of the fluid qualitatively as well as quantitatively. There are two general approaches in analyzing the fluid motion. In the first method (Lagrangian approach), the individual fluid particles are considered and their properties are studied as a function of time. In the second method (Eulerian approach), the ‘field’ concept is introduced and the properties are completely prescribed as the functions of space and time. In other words, the attention is focused at fixed points in space as the fluid passes those points. Velocity and Acceleration Field Since the ‘continuum’ assumption holds well for fluids, the description of any fluid property (such as density, pressure, velocity, acceleration etc.) can be expressed as a function of location. These representation as a function of spatial coordinates is called as “field representation” of the flow. One of the most important fluid variables is the velocity field. It is a vector function of position and time with components uv, and w as scalar variables i.e. V=++ u( xyzt,,,) iˆˆ v( xyzt ,,,) j w( xyzt ,,,) kˆ (3.1.1) The magnitude of the velocity vector i.e. V=( uvw22 ++ 2) , is the speed of fluid. The total time derivative of the velocity vector is the acceleration vector field (a) of the flow which is given as, dV d{ u( xyzt,,,)} d{ v( xyzt ,,,)} d{ w( xyzt,,,)} a==++ ijkˆˆ ˆ (3.1.2) dt dt dt dt Joint initiative of IITs and IISc – Funded by MHRD Page 1 of 56 NPTEL – Mechanical – Principle of Fluid Dynamics For instance, the scalar time derivative of u is expressed as, d{ u( xyzt,,,)} ∂∂u u dx ∂ u dy ∂ u dz =+++ dt∂∂ t t dt ∂ t dt ∂ t dt ∂∂∂uuu ∂ u =+++uvw (3.1.3) ∂∂∂ttt ∂ t ∂u = +∇(Vu. ) ∂t When u is replaced with vwand in the above equation, then the corresponding expressions would be, d{ v( xyzt,,,)} ∂v =+∇(Vv. ) dt∂ t (3.1.4) d{ w( xyzt,,,)} ∂w = +∇(Vw. ) dt∂ t Now, summing them into a vector quantity, one may write Eq. (3.1.2) in compact form as, dV∂ V ∂∂ V V ∂∂ V V a= = + u + v + w = +∇( VV. ) dt∂ t ∂∂ x y ∂∂ z t (3.1.5) ∂∂ ∂ ∂∂∂ where, Vu= + v + w and ∇=iˆˆ + j + kˆ ∂∂xy ∂ z ∂∂ xy ∂ z ∂V In the above equation, is called as “local acceleration” and the second part i.e. ∂t ∂∂VV ∂ V uvw++ is called a “convective acceleration”. The total time derivative ∂∂xy ∂ z is called as “substantial/material” derivative. This field concept can be applied to any variable (vector or scalar). For example, one may write the total derivative for pressure and temperature field as, dp∂ p ∂∂ p p ∂∂ p p = +u + v + w = +∇( Vp. ) dt∂ t ∂∂ x y ∂∂ z t (3.1.6) dT∂ T ∂∂ T T ∂∂ T T = +u + v + w = +∇( VT. ) dt∂ t ∂∂ x y ∂∂ z t Joint initiative of IITs and IISc – Funded by MHRD Page 2 of 56 NPTEL – Mechanical – Principle of Fluid Dynamics Visualization of Fluid Flow The quantitative and qualitative information of fluid flow can be obtained through sketches, photographs, graphical representation and mathematical analysis. However, the visual representation of flow fields is very important in modeling the flow phenomena. In general, there are four basic types of line patterns used to visualize the flow such as timeline, pathline, streakline and streamlines. Regardless of how the results are obtained, (i.e. analytically/experimentally/computationally) it is necessary to plot the data to get the feel of flow parameters that vary in time and/or shape (such as profile plots, vector plots and contour plots). (a) Timeline: A ‘timeline’ is a set of fluid particles that form a line at a given instant (Fig. 3.1.1-a). Thus, it is marked at same instant of time. Subsequent observations of the line provide the information of the flow field. They are particularly useful in situations where uniformity of flow is to be examined. (b) Pathline: It is the actual path traversed by a given fluid particle as it flows from one point to another (Fig. 3.1.1-b). Thus, the pathline is a Lagrangian concept that can be produced in the laboratory by marking the fluid particle and taking time exposure photograph of its motion. Pathlines can be calculated numerically for a known velocity field (V ) i.e. tend = + x xstart ∫ V dt (3.1.7) tstart (c) Streakline: A streakline consists of all particles in a flow that has previously passed through a common point (Fig. 3.1.1-c). Here, the attention is focused to a fixed point in space (i.e. Eulerian approach) and identifying all fluid particles passing through that point. These lines are laboratory tool rather than analytical tool. They are obtained by taking instantaneous photographs of selected particles that have passed through a given location in the flow field. Joint initiative of IITs and IISc – Funded by MHRD Page 3 of 56 NPTEL – Mechanical – Principle of Fluid Dynamics (d) Streamline: These are the lines drawn in the flow field so that at a given instant, they are tangent to the direction of flow at every point in the flow field (Fig. 3.1.1-d). Since the streamlines are tangent to the velocity vector at every point in the flow field, there can be no flow across a streamline. Mathematically, these lines are obtained analytically by integrating the equations defining lines tangent to the velocity field. In a two dimensional flow field as shown in the figure, the slope of the streamline is equal to the tangent of the angle that velocity vector makes with x-axis i.e. dy v = (3.1.8) dx u This equation can be integrated to obtain the equation of streamlines. When bundles of streamlines are considered in a flow field, it constitutes a ‘stream tube’ (Fig. 3.1.1-e). Since streamlines are everywhere parallel to the local velocity, fluid cannot cross a streamline, so fluids within a stream tube remain there and cannot cross the boundary at stream tube. Fig. 3.1.1: Basic line patterns in fluid flow: (a) Timelines; (b) Pathline; (c) Streakline; (d) Streamline; (e) Streamtube. Joint initiative of IITs and IISc – Funded by MHRD Page 4 of 56 NPTEL – Mechanical – Principle of Fluid Dynamics The following observations can be made about the fundamental line patterns; 1. Mathematically, it is convenient to calculate a streamline while other three are easier to generate experimentally. 2. The streamlines and timelines are instantaneous lines while pathlines and streakline are generated by passage of time. 3. In a steady flow, all the four basic line patterns are identical. Since, the velocity at each point in the flow field remains constant with time, consequently streamline shapes do not vary. It implies that the particle located on a given streamline will always move along the same streamline. Further, the consecutive particles passing through a fixed point in space will be on the same streamline. Hence, all the lines are identical in a steady flow. They do not coincide for unsteady flows. (f) Graphical data analysis techniques: Profile plots, vector plots and contour plots are few important techniques in which fluid flow properties can be analyzed. The profile plot (Fig. 3.1.2-a) indicates the variation of any scalar property (such as pressure, temperature and density) along some desired direction in a flow field. Using this plot, it is possible to examine the relative behavior of all variables in a multivariate data set. Fig. 3.1.2: Graphical representation of data analysis technique: (a) profile plot, (b) vector plot, (c) contour plot. Joint initiative of IITs and IISc – Funded by MHRD Page 5 of 56 NPTEL – Mechanical – Principle of Fluid Dynamics A vector plot (Fig. 3.1.2-b) is an array of arrows indicating the magnitude and direction of a vector property at an instant of time. Although, streamlines indicate the direction of instantaneous velocity field, but does not directly indicate the magnitude of velocity. A useful flow pattern for both experimental and computational fluid flow is the ‘vector plot’ that indicates the magnitude and direction of instantaneous vector property. A contour plot (Fig. 3.1.2-c) is a two-dimensional plot of a three-dimensional surface showing lines where the surface intersects planes of constant elevation. Thus, they are curves with constant values of scalar property (or magnitude of vector property) at an instant of time. They can be filled in with either colors or sheds of gray representing the magnitude of the property. Joint initiative of IITs and IISc – Funded by MHRD Page 6 of 56 NPTEL – Mechanical – Principle of Fluid Dynamics Module 3 : Lecture 2 INVISCID INCOMPRESSIBLE FLOW (Kinematic Description of Fluid Flow) In order to illustrate this concept, we consider a typical fluid element of certain volume at any arbitrary time as shown in Fig. 3.2.1. After certain time interval, it has moved and changed its shape as well as orientation drastically. However, when we limit our attention to an infinitesimal particle of volume dV(= δδδ x.