addition we will assume that the material only undergoes small deformation and that this deformation is proportional to the applied 12.4 Elementary strain The longitudinal, or axial, s
Trang 1216 Introduction to continuum mechanics
the device would give a reading for a specific point in space and does not follow a particular particle of fluid A flow velocity device would also
be attached to the pipe
A system of co-ordinates which relates prop- erties to a specific point in space is known as Eulerian Thus pressure p is a function of x and
time t
The particle velocity is here defined by
dr
dt
Consider first how measurements of deforma-
tion are made for the pipe itself TO determine note here that the partial derivative is not how much the material has been stretched we required, however the velocity will be a function could measure the relative movement of two of both x and t
marks, one at x = xA and the other at x = xB In summary, Lagrangian co-ordinates refer to a Note that if the Pipe moves as a rigid body the particular particle whilst Eulerian co-ordinates marks will move with the pipe SO the marks will refer to a particular point in space
not be at their original locations We must regard
XA and XB as being the ‘names’ of the marks: that 12.6 Ideal continuum
is they define the original positions of the marks An ideal solid is defined as one which is
In this context x does not vary, SO we must use a homogeneous and isotropic, by which we mean different symbol to denote the displacement of that the properties are uniform throughout the the marks from their original positions The region and SO not depend on orientation In symbols uA and uB will be used addition we will assume that the material only
undergoes small deformation and that this deformation is proportional to the applied
12.4 Elementary strain
The longitudinal, or axial, strain is defined to be
loading system This last statement is known as the change in length per unit length
Hooke’s law
thus the strain I = ~ (12-2) isotropic and the term is usually restricted to
incompressible, inviscid fluids This is clearly a
XB - X A
As the distance between the marks approaches to good approximation to the properties of water in
and the effects of viscosity are confined to a thin (12.3) layer close to a solid surface known as the
boundary layer For gases such as air, which are The partial differential is required since strain very compressible, it is found that the effects of could vary with time as well as with position compressibility in flow processes are not signi-
ficant until relative velocities approaching the
12.5 Particle velocity
The velocity of a particle at a given value of x, say ’peed Of sound are reached
x A , is simply
12.7 Simple tension
au
E = -
ax
v = - dU
Again the partial derivative is used to indicate
that x is held constant
The above co-ordinate system is known as
Lagrangian
If we are concerned with the fluid in the pipe
then a pressure measuring device would be fixed
to the pipe and, assuming that the pipe is rigid,
Figure 12.2 shows a straight uniform bar length L ,
cross-section area A and under the action of a
Trang 212.9 The control volume 217
tensile force F The state of tension along the bar
surface is F to the right and on a left-facing
d2U
is constant, this means that if a cut is made ( F + E & ) - F = ( P A & ) ,
at
anywhere along the bar the force on a right-facing
surface it is F to the left
It follows that at any point the tensile load
divided by the original cross-section area, F / A , is
constant and this quantity is cajled the stress (+ A
negative stress implies that the load is compres-
aF d2U
Since nominal o r engineering stress is defined as force/original area, then dividing both sides of equation 12.8 bY A gives
ax
sive If the extension under this load is 6 then the a a a2u
ax
By Hooke’s law 6 m F so E ~c a or
We have already shown that the strain
a U
property of the material known as Young’s ax
modulus
Re-arranging the above equations gives
so substituting 12.11 into 12.9 and using 12.10 we (12.7) finally obtain
FL
a=
A E
a2u a2u
a x 2 at2
A state of tension resulting in an extension is
regarded as being associated with a positive stress
and a positive strain (See Appendix 8 f o r a
discussion of material properties )
Figure 12.3 shows an element of a uniform bar
which has no external loads applied along its
length, the external loads or constraints occurring
only at the ends The material is homogeneous the solution of which is u = a + bx where a and b
with a density P l Young’s modulus E and a are constants depending on the boundary
conditions
constant cross-section area A
du
dx
This is a very common equation in applied physics and is known as the wave equation
In a statics case the right-hand side of equation 12.12 is zero so that u is a function of x only,
d2 u
- = o
dx2
Now strain
E = - = b = V I E = ( F / A ) / E
so if at x = 0 u = 0 then a = 0, u = Fx/(AE) At
x = L the displacement is equal to F L / ( A E ) , as
expected
12.9 The control volume
The equations of motion developed for rigid bodies and commonly used for a solid continuum refer t o a fixed amount of matter However for fluids it is usually more convenient to concentrate
on a fixed region of space with a volume V and a
surface S The properties of the fluid are expressed as functions of spatial position and of time, it being noted that different particles will occupy a given location at different times
The mass of an element of length dx is pAdx
and this is constant as these quantities refer to the
original values
Resolving the forces in the x direction and
equating the net force to the mass of the element
times its acceleration gives
Trang 3218 Introduction to continuum mechanics
p by pv in the development of the continuity equation This is possible since p is the mass per unit volume and pv is the momentum per unit volume Thus the change in momentum in time At
is
a(pv) d V
AG = [I, pv ( v - &) + 1, at ]
AG Now force F = limAt-o-
At
= [ p ( v - d S ) + [ " Y d V (12.14)
5
A t time t the control volume is shown in
Fig 12.4 by the solid boundary A t time t + At the 12.12 Streamlines
position of the set of particles originally within the A streamline is a line drawn in space at a specific
control volume is indicated by the dashed time such that the velocity of the fluid at that
The velocity of the fluid at an elemental part of The distance along the streamline is s and, as in the surface is z, and the outward normal t o the path co-ordinates, e, is the unit tangent vector and
At the elemental surface area, dS, the increase
in mass in the time At is
p(dSvAtcosa) = pv-e,dSAt = pv-dSAt
Note that the area vector (dS = e n d s ) is defined
as having a magnitude equal to the elemental
surface area and a direction defined by the
outward normal unit vector, e,
Integrating over the whole surface we obtain
the net total mass gained by the original group
due to the velocity at the surface In addition to
this there is a further increase in mass due to the
density over the whole volume changing with
time
Thus the change in mass,
ds
dt Thus v = vet = - e,
Am = [ I s p v - d S + Iv$dV]At If the flow is steady, that is the velocity at any
point does not vary with time, a streamline is also
a path line
12.10 Continuity
Since the mass must remain constant
- = [ s p v - d S + [ ? d V = O (12.13) volume
this is known as the continuity equation a finite volume We now wish to obtain an
expression for an elemental volume correspond-
T o obtain the equations of motion we need to Figure 12.6 shows a rectangular element with consider the time rate of change in linear sides dx, dy and dz Considering the continuity
momentum This is achieved by simply replacing
Equation of motion for a fluid
equation we first evaluate the surface integral
Trang 412.14 Euler’s equation for fluid flow 219
component of velocity u since the streamlines at this surface may be diverging
A stream tube could have been used where the curved surface is composed of streamlines, but this means that the cross-section area would be a variable and the effect of pressure on this surface would have to be considered
\,pu-dS = [ pvx+-dx a 2 ] dydz-pv,dydz
[ a:1
+ pvy+-dy dzdx-pvydzdx
+ pv,+-dz dxdy-pv,dxdy
First we need to apply the continuity equation
- -
- [ apvx +- apvy + ””.I & dy dz so with reference to Fig 12.7
The vector operator V is defined, in Cartesian
(p+$ds)(v+E*)dA co-ordinates, to be
aP
at
V = i- + j - + k -
ax ay az
Neglecting second order terms
SO with pu = ipv, + jpv, + kpv,
l , p u d S = V-pudxdydz p-dV+ as v- d V + p u d S + - d V = dS at 0 (12.16)
where dV = dsdA
In applying the force equation we are going to include a body force, in this case gravity, in addition to the pressure difference Resolving
The operation V (pu) is said to be the divergence
of the pv field and is often written as div(pu)
Also [ v 2dV=-dxdydz at a t forces along the streamline
so the complete continuity equation is
aP
d F = p d A - p+-ds ( E ) dA
or
or
d F = pgcOSa dsdA (12.17)
In applying the momentum equation we shall
choose a small cylindrical element with its axis
surface, of area dS ’, there could be a small radial
(12.15)
aP
at
v*pu+- = o
equation 12.14, along a streamline However at the curved d G = ( p + g d s ) ( V + % d s ) av 2 dA-pvudA
Trang 5220 Introduction to continuum mechanics
= 2pv-dsdA +v2-dsdrdA +puudS’
The right-hand side of this expression can be
simplified by subtracting v times equation 12.16 to
give
combining with 12.17 and dividing through by
dsdA
and finally re-arranging gives
1 ap av av -gcosa - = v- +-
p as as at (12.18) This is known as Euler’s equation for fluid flow
Since v = v(s, t ) ,
dv av ds av dt av av
dt as dt at dt as at
- - - - - + =-v+-
the right-hand side of 12.18 may be written as
dv
dt
-
If we consider the case for steady flow where the
velocity at a given point does not change with
time, Euler’s equation may be written
1 do dv
the partial differentials have been replaced by
total differentials because v is defined to be a
function of s only Multiplying through by ds and
integrating gives
-I gcosads- I - - - - +constant
now cos ads = dz thus
I f + + g z = constant
If p is a known function of p then the integral can
be determined but if we take p to be constant we have
+ ”’ + gz = constant
this is known as Bernoulli’s equation
This equation is strictly applicable to steady flow of a non-viscous, incompressible fluid; it is, however, often used in cases where the flow is changing slowly The effects of friction are usually accounted for by the inclusion of experimentally determined coefficients As has already been
mentioned, the effects of compressibility can often be neglected in flow cases where the relative speeds are small compared with the speed of sound in the fluid
SECTION B Two- and three-dimensional continua
We are now going to extend our study of solid continua to include more than one dimension In our treatment of one-dimensional tension o r compression we did not consider any changes in the lateral dimensions Although we are going to use three dimensions we shall restrict the analysis
to plane strain conditions By plane strain we mean that any group of particles which lie in a plane will, after deformation, remain in a plane
It is possible that the plane will be displaced from the original plane but will still be parallel to it
It is an experimental fact that a stress applied in one direction only will produce strain in that direction and also at right angles to the stress axis
If a specimen is strained within the x-y plane then, if the strain in the z direction is to be zero, there must be a stress in the z direction as well as
in the x and y directions Conversely, if stresses are applied in the x and y directions with a zero stress in the z direction, there will be a resulting strain in the z direction as well as those in the x
and y directions The two-dimensional analyses presented later are based on the latter case
Trang 612.17 Poisson’s ratio
If Hooke’s law is obeyed, then the transverse
strain produced in axial tension will also be
proportional to the applied load; thus it follows
that the lateral strain will be proportional to the
axial strain The ratio
transverse strain
axial strain
- - v
where v is known as Poisson’s ratio
If a uniform rectangular bar, as shown in Fig
12.8, is loaded along the x axis then
E, = u x / E
E~ = -vu,/E
and E, = - v c , / E
12.1 8 Pure shear
Figure 12.9 shows a rectangular element which is
deformed by a change in shape such that the
length of the sides remain unaltered The shear
strain yxy is defined as the change in angle
(measured in radians) of the right angle between
adjacent edges This is a small angle consistent
with our discussion of small strains
12.19 Plain strain 221
Figure 12.10
This shows the equivalence of the complementary shear stresses
Again by Hooke’s law, shear stress is proportional to the shear strain
where G is known as the Shear Modulus or as the Modulus of Rigidity
-
Referring to Fig 12.11 it is seen that the shear strain can be expressed in terms of partial differential coefficients as
Yxy = Y1+ Y2
auy au,
ax ay
yxy = - +-
12.19 Plane strain
The rectangular element, shown in Fig 12.12, has one face in the XY plane and is distorted such that
the corner Points A , B , c and D rnOve in the XY
plane only
The translation of point A is u and that of point
C is u + du For small displacements
( 12.23)
The loading applied to the element to produce
pure shear is as shown in Fig 12.10 This set of
forces is in equilibrium, SO by considering the sum
of the moments of the two couples in the xy plane
(12.m) F,dr-F,dy=O
rXy = F,/(dydz)
The shear stress is defined as
d u = -dx+-dy i+ 2dx+Ldy
Substitution into equation 12.20 gives or in matrix form
Trang 7222 Introduction to continuum mechanics
au, au,
[:::I= k 4 [;] (12.24)
Let us now introduce the notation
Figure 12.13
1 au
xy 2 ( ax $)
(see Fig 12.13)
The 112 in the strain matrix spoils the simplicity
of the notation therefore it is common to replace
Figure 12.12
a u x -
aY
4Yxy by Exy
~ - u , , ~ etc
In this notation the strain in the x direction 12.20 Plane stress
The triangular elements shown in Fig 12.14 are in equilibrium under the action of forces which have components in the x and y directions but not in the z direction Note that the surface abcd has
area dydzi and area abef has an area dxdzj; these
are the vector components of the area e’f’c’d’
The sense of the stress component, shown on the diagram, is such that when multiplied by the area
vector it gives the force vector
Ex, = ux,x
similarly EYY = UY,Y
and the shear strain
and equation 12.24 becomes
yxy = uy,x + u , , ~
[::;
I = I [::: [;I :;::]
The square matrix can be written as the sum of a
symmetrical and an anti-symmetrical matrix By
this means the shear strain can be introduced
I
1
+ [ặx,y - uy,x) 0
u x , x I ( u x , y + uy,x 1
0 -%uy,x- UXJ [I::: :::I 7 [ l ( u x , y + uy,x)
[::;
UY 3 Y
therefore
Resolving in the x direction we obtain
+[lY -?I} [;I (12-25) where Oxy is the rigid body rotation in the xy
plane given by
F, = u,dydz+ rxydxdz
Fy = c,dxdz+ rxydydz
or, in matrix form,
Trang 8dy dz
[ :] = [ rz :][ dxdz]
Letting dydz = S, and dxdz = S,
In many texts rXy is replaced by mxy
The values of the components of stress and strain
depend on the orientation of the reference axes
In Fig 12.15 the axes have been rotated by an
angle 8 about the z axis
12.22 Principal strain 223
they may now be transformed by use of the transformation matrix
12.22 Principal strain
Since (du) = [T](du’) and (dx) = [TI(&’) we can write
[TKdu’) = (1.1 + [aLIWl(d4
(du‘) = [TIT{[El + [filI[Tl(dx’)-
and pre-multiplying by [TIT we obtain
The rotation [a] is not affected by the change
in axes because they are rotated in the xy plane The transformed strain matrix is
[&’I = [TIT[&] IT1
- cos0 sin8 E,,
[-sin e cos e ] [ E,, 2::]
cos0 -sine
x [ sine cos@
= [I:; 3
-
1
where
E’ ,, = E,, cos2 e + E,, sin2 e
E’,, = E , ~ C O S ~ e + &,sin2 e
E’,, = ( E ~ - ~,,)sinBcose
( E y y - E x x )
x = x’cos8-y’sine
which, in matrix form, becomes
(x) = ITl(x‘>
+ E,, (cos’ e - sin2 e)
-
- sm28+ E , , C O S ~ ~ (12.30) also (E’,,+ E ’ ~ , ) = ( E , + E ~ ) (12.31) From equation 12.30 it is seen that it is possible
(12.27)
2
or, in abbreviated form
The matrix [T1 is a transformation matrix It is
inversion that the inverse of this matrix is the
same as its transpose
easily shown from the geometry or by matrix to choose a va1ue for 8 such that &’xy = 0- The
value of 8 is found from
(12.32)
The axes for which the shear strain is zero are Writing equations 12.25 and 12.26 in abbrevi- known as the principal strain axes Let us
therefore take our original axes as the principal axes, that is E,, = 0 The longitudinal strains are now the principal strains and will be denoted by E~
in the x direction and by E~ in the y
2Exy
( E , - Eyy 1
tan28 =
I
cose sin8 -sine cos6
[TI-’ = [TIT = [
ated form as
(du) = {[El + [a1 I (k )
and ( F ) = [u](S)
Trang 9224 Introduction to continuum mechanics
From equations 12.28 and 12.29 we now have expressed in terms of rotated co-ordinates we
may write
(Ef,-&’ ) ( E 1 - E 2 ) ~ ~ ~ 2 e
f l =
thus [ T ] ( F ’ ) = [a][T](Sf)
so pre-multiplying by [TIT gives
and from equation 12.30
( E ~ - ~ ~ ) s i n 2 8
[of] = P I T [a1 [TI
- E l x y =
A simple geometric construction, known as
strains and the angle 8 Figure 12.16 shows a
axis, the ordinate being the negative shear strain
The location of the centre is given by the average
strain, and the radius of the circle is half the
difference between the principal strains It is seen
that this diagram satisfies the above equations
therefore Mohr’s circle, gives the relationship between the
circle plotted with its centre on the normal strain cos0 sin8 a,, aXy
[-sine wse][uxy uy,]
cos0 -sine
.[ sin8 cos0
-
-
I
where
a’ xx = a,, cos2 e + cry, sin2 e
urYy = uyy cos2 e + a,, sin2 e
dXy = (ayy - u,,) sin ecos e
+ aXy2cosBsin 8 (12.33)
- uxy2cosBsin8 (12.34)
+ oxy (cos2 e - sin2 e)
2
- (uyy - uxx) sin 28 + a,, cos20 (12.35)
also (a’,, + dYy) = (a, + uyy)
From equations 12.33 and 12.34 we now have
(ufxx - utyy) - (ul - u 2 ) ~ ~ ~ 2 e
-
and from equation 12.35
(ul -u2)sin28
2
-(+Ixy =
The form of these equations is the same as those for strain therefore a similar geometrical construction can be made, which is Mohr’s circle for stress as shown in Fig 12.17
Because we have taken the material to be isotropic it follows that the principal axes for stress coincide with those for strain This is because normal stresses cannot produce shear strain in a material which shows no preferred directions
Figure 12.16
It can be seen that when 6 = 7d4 the shear
strain is maximum and the normal strains are
equal If the circle has its centre at the origin then
for 0 = 7r/4 the normal strains are zero So for the
case of pure shear the principal strains are equal
and opposite with a magnitude E,, = y,,/2
In the case of uniaxial loading E~ = - vsl hence
the radius of the circle is ( E ~ + m1)/2 which also
equals the maximum shear strain at 8 = 7~14
so y x , = E , ( l + v ) = u l ( l + Z ) ) / E
Equation 12.26 can also be written in abbreviated
form as
( F ) = [ m )
and since the components of any vector can be
Trang 1012.24 The elastic constants 225
Because of the symmetry b must be equal to c so
we can write
~1 = ( b + ( ~ - b ) ) ~ i + b ~ 2 + 6 ~ 3
or u1 = ~ ( E ~ + E ~ + E ~ ) + ( U - ~ ) E ~
Let b = A and (a - b ) = 2 p where A and p are the Lame constants, and introducing dilatation A, the
sum of the strains, we have
and again because of symmetry
12.24 The elastic constants
So far we have encountered three elastic
constants namely Young's modulus ( E ) , the shear
modulus ( G ) and Poisson's ratio (v) There are
three others which are of importance, the first of
which is the bulk modulus
For small strains the change in volume of a
rectangular element with sides dx, dy and dz is
(&xx &I dY dz+ (&yydY ) dzdx + (E==dZ) dxdY- Figure 12-18
The volumetric strain, also known as the
dilatation, is the ratio of the change in volume to
the original volume; thus the dilatation
A = E,, + eyy + E, Let us now consider the case of pure shear, see
Fig 12.18- We have already Seen that (+I = - ~ X Y 9
a 2 = r x y , s1 = - E , ~ and E~ = e,y so substituting into equations 12.37 and 12.38 we have
It should be remembered that shear strain has no
effect on the volume
The average stress
a,,, = ( a x , + c y , + a, 113 - r x y = h A + 2 p ( - ~ , ~ )
rxy = AA + 2 p X y
and the bulk modulus K is defined by and
Solving the last two equations shows that A = 0
and rxy = 2peXy giving
Now consider the case of pure tension, see
Fig- 12-19> such that u z = 0 and E z = - V E I
(12.36) (For fluids the average stress is the negative of the
pressure p )
The two other constants are the Lame
constants and they will be defined during the
following discussion
In general every component of stress depends
consider an element which is aligned with the
principal axes of stress and strain, then each
principal stress will be a function of each principal
f l a w = KA
2Exy Y x y
linearly on each component of strain If we Substitution into equations 12.38 and 12.39 gives
~1 = AA + 2 ~ ~ 1
0 = AA- ~ / A v E ~