Course 1. Introduction. Fundamental Concepts of Rheology
Course 1. Introduction. Fundamental Concepts of Rheology
Course 1. Introduction. Fundamental Concepts of Rheology
- Heraclitus de
Samos
Everything will flow if you
wait long enough
Science of the flow and deformation of all forms of matter
was proposed by Bingham and Reiner accepted by American
Society of Rheology in 1929.
The origin comes from Greek words: rheos the river,
flowing, streaming and logos science.
Course 1
Fundamental concepts of
rheology
A rheological mathematical
model is presented by
a mathematical equation.
Constitutive equations/rheological equation of
state - mathematical equations/functions between
shear stresses/shear forces, strains/deformations or
shear rates and the material properties which describe
the material behavior.
In complex materials these equations may include
variable such as time, temperature and pressure.
Course 1
Fundamental concepts of
rheology
Rheological behavior
depends on:
-
Fundamental concepts of
rheology
Aim of Rheology
To explain the rheological properties and
measurement techniques
- To determine the behavior of fluids/materials under
a known load (e.g. ideal plastic, elastic or viscous,
viscoelastic, viscoplastic etc.)
To establish correlations between rheological
properties and composition/structure of materials
- To determine the change of rheological properties
during heating and cooling.
-
Course 1
Course 1
concrete technology,
soil mechanics,
polymers
dispersion,
-
and
composites,
point
flow
blood, bioengineering,
electro-rheology,
food
and
pharmaceutical
and
pigment
Course 1 cosmetics
products,
and
Course 1
Course 1
10
Displacement components of M to
M1 before movement: ux, uy, uz
Displacement components of N to
N1 after movement : ux, uy, uz
Assuming that the function of
deformation is continuous (the
Taylors series can be written):
u x' u x
u 'y u y
u z' u z
Course 1
u x
du
du
dx x dy x dz
dx
dy
dz
u y
dx
dx
du y
dy
dy
du y
dz
dz
u z
du
du
dx z dy z dz
dx
dy
dz
11
x
x 11
x
dx
x
ad
u y
y 22
a1b2 ab
ab
dy
u y
y
dy
y
u z
dz
u
z
z 33
z
dz
z
Deformation of a parallelepipeds
side.
Course 1
12
Deformation of the
parallelepipeds side.
b2b1
a1b2
y
y
y
u
u
1 y
dy y dy 1 y
y
y
tg
(for
small
angles)
y 1
u x
y
u y
and
x
Course 1
13
u x
u y
dy
dx
1
1 du x du y
y
dx
2
dy
dx
2 dy
dx
and than:
zx
1 du z du x
2 dx
dz
yz
1 du y du z
2 dz
dy
General expression:
ij
1 du i du j
1
ij
2 dj
di
2
i, j = 1, 2, 3.
Course 1
14
1
1
xy xz
2
2
1
1
yx y
yz
2
2
1
1
zx zy z
2
2
x xy xz
ij yx y yz
zx zy z
Dou to
reciprocity:
x xy xz
ij
y yz
z
1 V 1
m
x y z
3 V
3
Course 1
15
ij 0 m 0
0 0 m
( x m ) xy
xz
ij
( y m ) yz
( z m )
Course 1
16
F
A
Volume element
separated from a
continuous medium
and typical stresses
xx xy xz
ij
xy yx
zx xz
etc.
yy yz
zz
1
m ( x y z )
3
xz zx
p0 0
00
ij
0 p0 0
ij 0 0 0
000
0 0 p0
xx 0
ij
yy 0
0 zz
Course
1
18
Fundamental concepts of
rheology
3. SHEAR RATE (shear gradient, velocity gradient, strain
rate or rate of deformation)
(gradient de vitez sau reopanta)
Two-Plates-Model
s
1.
ds ds
d dh dt dv
const.
dt dt dh dh
dh
const.
v(h)
is
(1/s),
dh
called
19
Fundamental concepts of
rheology
Calculation of shear rates of technical processes
a. Buttering bread
v
0.1
v = 0.1 m/s
100(s 1 )
h 0.001
h = 1 mm = 0.001 m
b. Painting with a brush
v = 0.1 m/s
h = 100 m = 0.0001 m
v
0.1
1000(s 1 )
h 0.0001
10
(
m
/ s)
3
V = 1 l = 0.001 m
t
5
t = 5 s (filling time per bottle)
D = 10 mm, diameter of the circular
geometry of the injection
4Gv
4 2 10 4
2548(s 1 )
nozzle.
3
3
R
3.14 0.01
Course 1
20
Fundamental concepts of
rheology
Two-Plates-Model
2. Elastic deformation/strain
- The (shear) area A (m2) is
deflected by the (shear)
force F (N)
- The shear deformation
(also shear strain)
s
(%)
S=
0
Shear deformation of a
material in the shear
gap of two-plates-model
21
- Simple Shear (Forfecare simpl sau plan (A)) moving fluid layers
are flat and parallel - Flow between two parallel plates
- Rotational Shear (Forfecare de rotaie (B)) fluid layers are coaxial
cylinders that rotate at different speeds - Circular flow in the annular
gap between two coaxial cylinders,
- Telescopic shear (Forfecare telescopic (C)) fluid layers are coaxial
cylinders that slide at different speeds, parallel to their common axis Flow through capillaries, hoses, tubes or channels,
- Torsional shear (Forfecarea de torsiune (D)) fluid layers are
stacked disks that rotate at different speeds around their common axis
- Flow between a cone and plate or flow between two parallel plates.
Course 1
22
Fundamental concepts of
rheology
Shear rate tensor
Considering the rate:
wx
u x
t
d ij
x
j
d xx d xy d xz
d ij d yx d yy d yz
d zx d zy d zz
d ij
x i
d ij 2
d
ij
dt
dw i dw j
d du i
d du j
d du i
d du j
dt dx j dt dx i
dx j dt dx i dt
dx j dx i
d x dw x
dt
dy
d ii 2 ii
ij 2 ij
23
Pure Shear
0 xy 0
ij yx 0 0
0 0 0
Simple Shear
Shear
0 0 0
ij yx 0 0
0 0 0
Rotational
0 0
xy
ij yx 0 0
0 0 0
Course 1
24
dw x
xy
dy
Kinematic viscosity
(mm2/s)
xy
(dynamic
viscosity)
25
Fundamental concepts of
rheology
Shear modulus the reversible-elastic deformation range
(previously sometimes called modulus of elasticity in
shear or rigidity modulus) - the ratio of the shear
deformation:
stress and the corresponding
G
xx
xx
(Pa)
Course 1
26
Fundamental concepts of
rheology
Poissons coefficient correlates deformations caused by
normal strains into a single direction of the body, causing
elongation in the direction of application (x) and shrinking on
yy
the other two directions (y
or z):
xx
The majority of materials have: 0 < < 0.5. Materials with =0.5
are incompressible because the sum of all deformations lead to zero
volume changes.
Course 1
27
28
29