Monroe L. Weber-Shirk S chool of Civil and Environmental Engineering Basic Governing Differential Equations CEE 331 July 14, 2015 CEE 331 July 14, 2015

Overview ä Continuity Equation ä Navier-Stokes Equation ä (a bit of vector notation...) ä Examples (all laminar flow) ä Flow between stationary parallel horizontal plates ä Flow between inclined parallel plates ä Pipe flow (Hagen Poiseuille) ä Continuity Equation ä Navier-Stokes Equation ä (a bit of vector notation...) ä Examples (all laminar flow) ä Flow between stationary parallel horizontal plates ä Flow between inclined parallel plates ä Pipe flow (Hagen Poiseuille)

Why Differential Equations? ä A droplet of water ä Clouds ä Wall jet ä Hurricane ä A droplet of water ä Clouds ä Wall jet ä Hurricane

Conservation of Mass in Differential Equation Form Mass flux into differential volume Mass flux out of differential volume Rate of change of mass in differential volume

Continuity Equation Mass flux out of differential volume Higher order term out in Rate of mass decrease 1-d continuity equation

u, v, w are velocities in x, y, and z directions Continuity Equation 3-d continuity equation If density is constant... Vector notation or in vector notation True everywhere! (contrast with CV equations!) divergence

Continuity Illustrated x y What must be happening? < >

Shear Gravity Pressure Navier-Stokes Equations momentum ä Derived by Claude-Louis-Marie Navier in 1827 ä General Equation of Fluid Motion ä Based on conservation of ___________ with forces… ä ____________ ä ___________________ ä U.S. National Academy of Sciences has made the full solution of the Navier-Stokes Equations a top priority ä Derived by Claude-Louis-Marie Navier in 1827 ä General Equation of Fluid Motion ä Based on conservation of ___________ with forces… ä ____________ ä ___________________ ä U.S. National Academy of Sciences has made the full solution of the Navier-Stokes Equations a top priority

If _________ then _____ Navier-Stokes Equation Inertial forces [N/m 3 ], a is Lagrangian acceleration Pressure gradient (not due to change in elevation) Shear stress gradient Navier-Stokes Equations Is acceleration zero when dV/dt = 0? g is constant a is a function of t, x, y, z NO!

Lagrangian acceleration Notation: Total Derivative Eulerian Perspective Total derivative (chain rule) Material or substantial derivative

xx Over what time did this change of velocity occur (for a particle of fluid)? Why no term? N-S

Application of Navier-Stokes Equations ä The equations are nonlinear partial differential equations ä No full analytical solution exists ä The equations can be solved for several simple flow conditions ä Numerical solutions to Navier-Stokes equations are increasingly being used to describe complex flows. ä The equations are nonlinear partial differential equations ä No full analytical solution exists ä The equations can be solved for several simple flow conditions ä Numerical solutions to Navier-Stokes equations are increasingly being used to describe complex flows.

Navier-Stokes Equations: A Simple Case ä No acceleration and no velocity gradients xyz could have any orientation Let y be vertical upward  g For constant 

Infinite Horizontal Plates: Laminar Flow Derive the equation for the laminar, steady, uniform flow between infinite horizontal parallel plates. y x Hydrostatic in y x y z

Infinite Horizontal Plates: Laminar Flow Pressure gradient in x balanced by shear gradient in y No a so forces must balance! Now we must find A and B… Boundary Conditions

negative Infinite Horizontal Plates: Boundary Conditions No slip condition u = 0 at y = 0 and y = a a y   let be___________ u u What can we learn about  ? x

Laminar Flow Between Parallel Plates U  a u y x No fluid particles are accelerating Write the x-component

Flow between Parallel Plates General equation describing laminar flow between parallel plates with the only velocity in the x direction u is only a function of y

Flow Between Parallel Plates: Integration U  a u y x

u = U at y = a Boundary Conditions Boundary condition u = 0 at y = 0

Discharge per unit width! Discharge

Example: Oil Skimmer An oil skimmer uses a 5 m wide x 6 m long moving belt above a fixed platform (  =60º) to skim oil off of rivers (T=10 ºC). The belt travels at 3 m/s. The distance between the belt and the fixed platform is 2 mm. The belt discharges into an open container on the ship. The fluid is actually a mixture of oil and water. To simplify the analysis, assume crude oil dominates. Find the discharge and the power required to move the belt. h l  = 1x10 -2 Ns/m 2  = 860 kg/m 3 60º x g

Example: Oil Skimmer In direction of belt q = m 2 /s (per unit width) Q = m 2 /s (5 m) = m 3 /s 0 0 dominates 60º x g

ä How do we get the power requirement? ä ___________________________ ä What is the force acting on the belt? ä ___________________________ ä Remember the equation for shear? ä _____________ Evaluate at y = a. ä How do we get the power requirement? ä ___________________________ ä What is the force acting on the belt? ä ___________________________ ä Remember the equation for shear? ä _____________ Evaluate at y = a. Example: Oil Skimmer Power Requirements Power = Force x Velocity [N·m/s] Shear force (   ·  L · W)   =   (du/dy)

Example: Oil Skimmer Power Requirements (shear by belt on fluid) = 3.46 kW FV How could you reduce the power requirement? __________ Decrease 

Potential and kinetic energy Heating the oil (thermal energy) Example: Oil Skimmer Where did the Power Go? ä Where did the energy input from the belt go? h = 3 m

Velocity Profiles Pressure gradients and gravity have the same effect. In the absence of pressure gradients and gravity the velocity profile is ________ linear

Example: No flow  Find the velocity of a vertical belt that is 5 mm from a stationary surface that will result in no flow of glycerin at 20°C (  = 0.62 Ns/m 2 and  =12300 N/m 3 )

Laminar Flow through Circular Tubes ä Different geometry, same equation development (see Young, et al. p 253) ä Apply equation of motion to cylindrical sleeve (use cylindrical coordinates) ä Different geometry, same equation development (see Young, et al. p 253) ä Apply equation of motion to cylindrical sleeve (use cylindrical coordinates)

Max velocity when r = 0 Laminar Flow through Circular Tubes: Equations Velocity distribution is paraboloid of revolution therefore _____________ _____________ Q = VA = average velocity (V) is 1/2 v max VR2VR2 R is radius of the tube

Laminar Flow through Circular Tubes: Diagram Velocity Shear (wall on fluid) True for Laminar or Turbulent flow Shear at the wall Laminar flow Next slide!

cv energy equation Relationship between head loss and pressure gradient for pipes Constant cross section l is distance between control surfaces (length of the pipe) In the energy equation the z axis is tangent to g x is in tangent to V x z

The Hagen-Poiseuille Equation Hagen-Poiseuille Laminar pipe flow equations From Navier-Stokes Relationship between head loss and pressure gradient What happens if you double the pressure gradient in a horizontal tube? ____________ flow doubles V is average velocity

Example: Laminar Flow (Team work) Calculate the discharge of 20ºC water through a long vertical section of 0.5 mm ID hypodermic tube. The inlet and outlet pressures are both atmospheric. You may neglect minor losses. What is the total shear force? What assumption did you make? (Check your assumption!) Calculate the discharge of 20ºC water through a long vertical section of 0.5 mm ID hypodermic tube. The inlet and outlet pressures are both atmospheric. You may neglect minor losses. What is the total shear force? What assumption did you make? (Check your assumption!)

Summary ä Navier-Stokes Equations and the Continuity Equation describe complex flow including turbulence ä The Navier-Stokes Equations can be solved analytically for several simple flows ä Numerical solutions are required to describe turbulent flows ä Navier-Stokes Equations and the Continuity Equation describe complex flow including turbulence ä The Navier-Stokes Equations can be solved analytically for several simple flows ä Numerical solutions are required to describe turbulent flows

Glycerin y

Example: Hypodermic Tubing Flow = weight!

Euler’s Equation Along a Streamline Inviscid flow (frictionless) x along a streamline v = u = velocity in x direction Velocity normal to streamline is zero

Euler’s Equation (Multiplying by dx converts from a force balance equation to an energy equation) We’ve assumed: frictionless and along a streamline Steady Euler’s equation along a streamline x is the only independent variable

Bernoulli Equation Euler’s equation The Bernoulli Equation is a statement of the conservation of ____________________ Integrate for constant density Bernoulli Equation Mechanical Energy p.e. k.e.

Hydrostatic Normal to Streamlines? y, v perpendicular to streamline (v = 0) x, u along streamline

Laminar Flow between Parallel Plates U q dldl a u y dydy q h l

Equation of Motion: Force Balance q pressure shear gravity acceleration = l

Equation of Motion But q h l Laminar flow assumption!

U q a u Limiting cases Both plates stationary Hydrostatic pressure Linear velocity distribution Parabolic velocity distribution Motion of plate Pressure gradient y x