'Fluid mechanics' is the branch of
continuum mechanics that studies
fluids, that is, liquids and gases. It can be further subdivided into
fluid statics, the study of fluids at rest, and
fluid dynamics, the study of fluids in motion. In the modern discipline called ''
Computational Fluid Dynamics'' (CFD), computational approach is used to develop solutions to fluid mechanics problems.
Relationship to continuum mechanics
Fluid mechanics is often considered a subdiscipline of
continuum mechanics, as illustrated in the following table.
| Continuum mechanics the study of the physics of continuous materials | Solid mechanics: the study of the physics of continuous materials with a defined rest shape. | Elasticity: which describes materials that return to their rest shape after an applied stress. |
| Plasticity: which describes materials that permanently deform after a large enough applied stress. | Rheology: the study of materials with both solid and fluid characteristics |
| 'Fluid mechanics': the study of the physics of continuous materials which take the shape of their container. | Non-Newtonian fluids |
| Newtonian fluids |
In a mechanic view, a fluid is a substance that does not support
tangential stress; that is why a fluid in rest has the shape of their containing vessel.
Assumptions
Like any mathematical model of the real world, fluid mechanics makes some basic assumptions about the materials being studied. These assumptions are turned into equations that must be satisfied if the assumptions are to hold true. For example, consider an incompressible fluid in three dimensions. The assumption that mass is conserved means that for any fixed closed surface (such as a sphere) the rate of mass passing from ''outside'' to ''inside'' the surface must be the same as rate of mass passing the other way. (Alternatively, the mass ''inside'' remains constant, as does the mass ''outside''). This can be turned into an
integral equation over the surface.
Fluid mechanics assumes that every fluid obeys the following:
★
Conservation of mass
★
Conservation of momentum
★ The continuum hypothesis, detailed below.
Further, it is often useful (and realistic) to assume a fluid is
incompressible - that is, the density of the fluid does not change. Liquids can often be modelled as incompressible fluids, whereas gases cannot.
Similarly, it can sometimes be assumed that the
viscosity of the fluid is zero (the fluid is ''inviscid''). Gases can often be assumed to be inviscid. If a fluid is viscous, and its flow contained in some way (e.g. in a
pipe), then the flow at the boundary must have zero velocity. For a viscous fluid, if the boundary is not porous, the shear forces between the fluid and the boundary results also in a zero velocity for the fluid at the boundary. This is called the
no-slip condition. For a porous media otherwise, in the frontier of the containing vessel, the slip condition is not zero velocity, and the fluid has a discontinuous velocity field between the free fluid and the fluid in the porous media (this is related to the
Beavers and Joseph condition).
The continuum hypothesis
Fluids are composed of
molecules that collide with one another and solid objects. The continuum assumption, however, considers fluids to be
continuous. That is, properties such as density, pressure, temperature, and velocity are taken to be well-defined at "infinitely" small points, defining a REV (Reference Element of Volume), at the geometric order of the distance between two adjacent molecules of fluid. Properties are assumed to vary continuously from one point to another, and are averaged values in the REV. The fact that the fluid is made up of discrete molecules is ignored.
The continuum hypothesis is basically an approximation, in the same way planets are approximated by point particles when dealing with celestial mechanics, and therefore results in approximate solutions. Consequently, assumption of the continuum hypothesis can lead to results which are not of desired accuracy. That said, under the right circumstances, the continuum hypothesis produces extremely accurate results.
Those problems for which the continuum hypothesis does not allow solutions of desired accuracy are solved using
statistical mechanics. To determine whether or not to use conventional fluid dynamics or statistical mechanics, the
Knudsen number is evaluated for the problem. The Knudsen number is defined as the ratio of the molecular
mean free path length to a certain representative physical length
scale. This length scale could be, for example, the radius of a body in a fluid. (More simply, the Knudsen number is how many times its own diameter a particle will travel on average before hitting another particle). Problems with Knudsen numbers at or above
unity are best evaluated using statistical mechanics for reliable solutions.
Navier-Stokes equations
''Main article: ''
Navier-Stokes equations''
The 'Navier-Stokes equations' (named after
Claude-Louis Navier and
George Gabriel Stokes) are the set of equations that describe the motion of
fluid substances such as liquids and gases. These equations state that changes in
momentum (
acceleration) of fluid particles depend only on the external
pressure and internal viscous forces (similar to
friction) acting on the fluid. Thus, the Navier-Stokes equations describe the balance of forces acting at any given region of the fluid.
The Navier-Stokes equations are
differential equations which describe the motion of a fluid. Such equations establish relations among the rates of change the variables of interest. For example, the Navier-Stokes equations for an ideal fluid with zero viscosity states that acceleration (the rate of change of velocity) is proportional to the derivative of internal pressure.
This means that solutions of the Navier-Stokes equations for a given physical problem must be sought with the help of
calculus. In practical terms only the simplest cases can be solved exactly in this way. These cases generally involve non-turbulent, steady flow (flow does not change with time) in which the
Reynolds number is small.
For more complex situations, such as global weather systems like El Niño or lift in a wing, solutions of the Navier-Stokes equations can currently only be found with the help of computers. This is a field of sciences by its own called
computational fluid dynamics.
General form of the equation
The general form of the Navier-Stokes equations for the conservation of momentum is:
:
where
★
is the fluid density,
:
is the
substantive derivative (also called the material derivative)
★
is the velocity vector,
★
is the body force vector, and
★
is a
tensor that represents the surface forces applied on a fluid particle (the
comoving stress tensor).
Unless the fluid is made up of spinning degrees of freedom like vortices,
is a symmetric tensor. In general, (in three dimensions)
has the form:
:
where
★
are normal stresses, and
★
are tangential stresses (shear stresses).
The above is actually a set of three equations, one per dimension. By themselves, these aren't sufficient to produce a solution. However, adding conservation of mass and appropriate boundary conditions to the system of equations produces a solvable set of equations.
Newtonian vs. non-Newtonian fluids
A 'Newtonian fluid' (named after
Isaac Newton) is defined to be a
fluid whose
shear stress is linearly proportional to the
velocity gradient in the direction
perpendicular to the plane of shear. This definition means regardless of the forces acting on a fluid, it ''continues to flow''. For example, water is a Newtonian fluid, because it continues to display fluid properties no matter how much it is stirred or mixed. A slightly less rigorous definition is that the
drag of a small object being moved through the fluid is proportional to the force applied to the object. (Compare
friction).
By contrast, stirring a
non-Newtonian fluid can leave a "hole" behind. This will gradually fill up over time - this behaviour is seen in materials such as pudding,
oobleck, or
sand (although sand isn't strictly a fluid). Alternativley, stirring a non-Newtonian fluid can cause the viscosity to decrease, so the fluid appears "thinner" (this is seen in non-drip
paints). There are many types of non-Newtonian fluids, as they are defined to be something that fails to obey a particular property.
Equations for a Newtonian fluid
''Main article:
Newtonian fluid''
The constant of proportionality between the shear stress and the velocity gradient is known as the
viscosity. A simple equation to describe Newtonian fluid behaviour is
:
where
:
is the shear stress exerted by the fluid ("
drag")
:
is the fluid viscosity - a constant of proportionality
:
is the velocity gradient perpendicular to the direction of shear
For a Newtonian fluid, the viscosity, by definition, depends only on
temperature and
pressure, not on the forces acting upon it. If the fluid is
incompressible and viscosity is constant across the fluid, the equation governing the shear stress (in
Cartesian coordinates) is
:
where
:
is the shear stress on the
face of a fluid element in the
direction
:
is the velocity in the
direction
:
is the
direction coordinate
If a fluid does not obey this relation, it is termed a
non-Newtonian fluid, of which there are several types.
See also
★
Applied mechanics
References
★ White, Frank M. (2003). ''Fluid Mechanics.'' McGraw-Hill. ISBN 0072402172
★ Cramer, Mark.
"The Gallery of Fluid Mechanics"
External link
★
CFDWiki -- the Computational Fluid Dynamics reference wiki.