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Conservation of Mass Often called ‘The Continuity Equation’ Conservation of Mass Often called ‘The Continuity Equation’

Conservation of Mass Often called ‘The Continuity Equation’ - PowerPoint Presentation

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Uploaded On 2023-10-04

Conservation of Mass Often called ‘The Continuity Equation’ - PPT Presentation

What is velocity not uniform Conservation of Linear Momentum General Case Fma Steady State Moment of Momentum Torque Power Work per Unit Mass Application from textbook U velocity of head due to angular rotation velocity of nozzle as measured relative to a fixed surface ID: 1023059

flow velocity conservation boundary velocity flow boundary conservation rotation cylindrical rate momentum nozzle equations steady relative component continuity formsteadyincompressible

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1. Conservation of MassOften called ‘The Continuity Equation’What is velocity not uniform

2. Conservation of Linear MomentumGeneral Case (F=ma)Steady State

3. Moment of MomentumTorquePowerWork per Unit Mass

4. Application (from textbook)U – velocity of head due to angular rotation (velocity of nozzle as measured relative to a fixed surface) - wRW – velocity of nozzle exit flow as viewed from the nozzle – Q/AV – fluid velocity as measured relative to a fixed control surface (typically what you need for formulas on previous slide)

5. Conservation of EnergyFor steady, incompressible flow with shaft work

6. Vorticity (Rotation)Counterclockwise rotation is positive (z component is component out of the page). Others, in x-y also existvorticity (zero => irrotational)Related, rate of shearing strain

7. Forms of Continuity EquationGeneral FormSteadyIncompressible

8. Cylindrical Polar CoordinatesGeneral FormSteadyIncompressible

9. StreamfunctionFor incompressible, plane two dimensional flow we can define a streamfunction psi, such thatQuantifies the flow rate between two streamlines (lines of constant psi)Cylindrical:

10. The Navier Stokes Equations

11. In Cylindrical Coordinates

12. Our assumptions2d (x-y or r-z or r-q)IncompressibleSteady State (d/dt=0)Fully Developed (d/dx=0 or d/dz=0 – except pressure)With these we are typically left with a 2nd order ordinary differential equation that we can readily solve.We then must apply boundary conditions for unknown constantsNo flow (velocity normal to a boundary is zero)No slip (fluivelocity tangential to a boundary is the same as the velocity of the boundary)

13. Momentum - Recipe Approach Draw Control VolumeIdentify all inlets and outletsIdentify all forces acting and their specific direction of action (break into x and y components)For each inlet and outlet calculate mass flow rate (rAv)For each inlet outlet identify velocity vector (v)Break velocity vector v into x and y componentsCombine last three steps to identify x and y components of momentum flux, i.e. v|xrAv and v|yrAvSubstitute into x and y momentum equations

14. Sample Problems

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20. Energy Equations

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