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Today’s Lecture Objectives:

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Presentation on theme: "Today’s Lecture Objectives:"— Presentation transcript:

1 Today’s Lecture Objectives:
Review (Learn) fluid dynamics Conservation equation Mass Momentum Energy

2 Terminology Fluid particle Scalar vs. Vector Boundary conditions
Steady State vs. Unsteady State Stream lines Gradient Lines Incompressible vs. Compressible fluids …… Examples

3 Stream Lines and Gradient lines
Wind Gradient Lines Temperature Jet airspeed

4 Steady-state vs. Unsteady-stat

5 Conservation equations
Fluid Dynamics: Conservation equations

6 Fluid particle vs Control Volume
Pay attention to the orientation of the coordinate system

7 Important operations Total derivative for fluid particle which is moving: V z any scalar y Vector and scalar operators: x scalar vector

8 Total Derivative Shows how variable  change during time while traveling from A to B Change in  are introduced by changing boundary conditions over time and by moving from part A to B B V z A mathematical definition y Total derivative allows all arguments vary x Physical interpretation …

9 Gradient of a scalar and Divergence of a vector
Where is the gradient of temperature largest? - nabla operator Divergence of a vector Vector filed You can also write that

10 Notation Density () in our problem change is so small that we can assume constant (most of the time) Book (handouts) vs. Class notes We are going to use these interchangeably Vx ≡ u Vy ≡ v Vz ≡ w

11 Continuity equation -conservation of mass
Mass flow in and out of fluid element Infinitely small volume Volume V = δxδyδz Volume sides: Ax = δyδz Ay = δxδz Az = δxδy Change of density in volume = = Σ(Mass in) - Σ(Mass out) ………………. same See equation 2.2 in notes = ….

12 Shear and Normal stress
τyx

13 Momentum equation –Newton’s second law
dimensions of fluid particle Stress components in x direction forces per unit of volume in direction x ……………….. ……………… ……………. total derivative

14 Momentum equation Sum of all forces in x direction Internal source
y direction z direction

15 Newtonian fluids Viscous stress are proportional to the rate of deformation (e) Elongation: Shearing deformation: For incompressible flow Viscous stress: viscosity

16 Momentum equations for Newtonian fluids
After substitution: x direction: y direction: z direction:

17 Momentum equations for Newtonian fluids
Same like previous slide with some rearrangements: x direction: y direction: z direction:

18 Momentum equations for Newtonian fluids
Finally: x direction: y direction: z direction:


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