Rheology Flashcards
1
Q
[sigma]
A
Shear stress
2
Q
[gamma]
A
Shear rate
3
Q
V
A
Velocity
4
Q
D
A
Distance
5
Q
n[eta]
A
Dynamic viscosity
6
Q
F
A
Force
7
Q
A
A
Area
8
Q
v[nu]
A
Kinematic viscosity
9
Q
p[rho]
A
Density
10
Q
[Phi]
A
Volume fraction
11
Q
M
A
Molecular weight
12
Q
R
A
Radius
13
Q
P
A
Pressure drop
14
Q
Define rheology
A
The study of the deformation and flow of matter
15
Q
Define viscosity
A
The viscosity of a liquid is its resistance to flow or move due to IMF.
Viscosity measure resistance to gradual deformation
E.g. Water has weak attractions between the molecules and low dynamic viscosity
Syrup has strong attractions between the molecules and higher dynamic viscosity
16
Q
Areas in pharmaceutics where rheology is important - fluids
A
Mixing Particle size reduction Passage through orifices (opening on body e.g. Mouth,rectum) Pumping Physical stability
17
Q
Areas in pharmaceutics where rheology is important - semisolid
A
Spreading and adherence to kin
Removal from jars or extrusion from tubes
Mixing of solids with miscible liquids
Release of drug base
18
Q
Areas in pharmaceutics where rheology is important - solids
A
Powder flow
19
Q
Areas in pharmaceutics where rheology is important - processing
A
Processing efficiency
20
Q
Define shearing rate and equation
A
Difference in velocity between layers
Shearing rate = dv/dr
(Velocity/difference) unit s-1
21
Q
Define newtons law
A
The rate of flow is directly related to the applied stress
22
Q
Shearing stress equation
A
F/A
23
Q
Dynamic viscosity equation
A
n = [sigma] / [gamma]
Nm-2 s or Pa s
24
Q
Define dynamic viscosity
A
The measure of the internal resistance or friction involved in the relative motion of one layer of molecules with respect to the next resulting from an applied force
25
Kinematic viscosity
Takes into account the density p of the liquid: v = n/p
| Unit: m2s-1 or stoke (S) cm2s-1
26
Define colloidal dispersion
One phase dispersed in another immiscible phase in the form of particles. E.g. Oil in water
27
Colloidal dispersion relative viscosity equation
nr = n/no
28
For colloidal dispersion the specific viscosity equation
nsp = n/no -1 = n-no/no = nr -1
```
n= viscosity of dispersion (dispersed phase plus solvent)
no = viscosity of the solvent
nsp = usually measure relative to a standard/reference liquid
```
29
Einstein equation
n = no (1+2.5 volume fraction)
```
n= viscosity of dispersion
no = viscosity of solvent
```
Specific viscosity is only dependent on volume fraction
30
Characteristics of Newtonian flow
Liquids are classified according to their flow type as either Newtonian or non Newtonian.
Newtonian fluids are simple fluids - linear relationship between shear stress and rate of shear (directly proportional otherwise it's non Newtonian), viscosity is not affected by shear rate
31
Boundary layer
Place of less stationary fluid. E.g. Water touching inside of tube will move slower than water water towards inside of the tube
32
Laminar flow
Flow between layer. When all materials move together
33
Transitional flow
Laminar to turbulent
34
Turbulent flow
Random
35
Reynolds number Re
```
Re= pvd/n
For tubular flow
If Re <2000 laminar flow
If Re >4000 turbulent flow
If 2000< Re <4000 depending on surface - if smooth laminar, if rough distributed
```
36
What does capillary viscometer measure
The flow time of a set volume of liquid between 2 marks at a given temperature
37
Hagen-Poiseuille equation for capillary viscometer
n= pi r4 tp / 8LV
```
r = radius of capillary
P = pressure difference between ends of tube
L = length of capillary
V = volume of the liquid
t = flow time
```
38
What is specific to a given viscometer
r L and V are specific to a given viscometer and can be combined together with pi into a constant k. P can be determined by measuring a reference liquid
Equation becomes n = kpt
Meaning if the time taken for a liquid to flow through the viscometer is greater the viscosity is higher
39
How does a falling sphere viscometer (Hoppler) obtain viscosity and what law applies
Obtains viscosity by messing the time it takes for a cylindrical or spherical object to fall through a sample over a specific distance
Stoke law applied (the diffusivity is inversely proportional to the viscosity)
40
Equation for stokes law
Sedimentation - stokes law
v = 2r2 (p2-p1) g / 9n
```
v is the velocity of sedimentation
r is radius of the spherical particle
p2 is density of the particle
p1 is density of the medium
n is viscosity
g is the acceleration of gravity
```
41
What particles does stokes law apply to and when can viscosity be calculated
Spherical
| Viscosity can be calculated after v is determined from the time needed to travel a certain distance
42
How does a rotational viscometer obtain viscosity
By turned a disc, bar or cylinder immersed in a liquid. The more viscous the liquid the stronger the resistance and hence higher the torque. Viscosity can be calculated from measured rotation speed vs applied torque
42
Define non Newtonian fluids
Complex pharmaceutical systems
Applied shear stress causes a change or interaction inside the system
Viscosity becomes non linear, it varies with shear rate
43
What are the 3 types of non Newtonian fluids
Plastic
Pseudo-plastic
Dilatant
44
Define plastic flow
Substance will not start to flow until a stress corresponding to the lower yield value is applied
45
Define pseudoplastic flow
Substance will start to flow immediately when stress is applied hence the curve passes through the origin. Viscosity decreases as shear rate increases
46
Define dilatant flow
Rarest of flow types. Materials increase in volume during shearing and exhibit shear thickening. Dilatant systems usually are suspensions containing high percentage of particles (>50%)
47
Apparent viscosity
napp used because shear rate calculated from tangent to curves in graphs
napp = shear stress (Pa) / shear rate (s-1)
For Newtonian fluids napp always remains the same
For non Newtonian fluids napp invariably changes
48
Shear thinning
Response of the system is non linear
Corresponding rate increases with stress and viscosity decreases
Pseudoplastic behaviour
49
Power law
[sigma]n = n' [gamma]
n' is the viscosity coefficient
n is the index of pseudo-plasticity or power law index
Take log on both sides of above equation
n log [sigma] = log n' + log [gamma]
log [gamma] = n log [sigma] - log n'
Linear relationship between log gamma and log sigma
50
Different flow systems have different n value
n = 1
n >1
n <1
n = 1 Newtonian flow
n >1 pseudoplastic flow
n <1 dilatant flow
51
Yield value
Ideal plastic is characterised by a yield value followed by ideal flow
At stresses below yield value the substance act as elastic materials
A typical folcculated suspension demonstrates plastic flow properties: it doesn't flow when shear is very low and starts to flow when shear is increased over certain value
52
Yield value
| Plastic flow can be described by
U = stress - f / shearing rate
f = yield value
Once yield value is exceeded the plastic viscosity changes proportionally with shearing stress resembling Newtonian flow
53
Causes for shear thinning
Changes inside a system which can lead to viscosity decreases:
- breaking of non covalent bonds (H bonds, charge interactions, hydrophobic interactions)
- alignment of molecules/polymers along the direction of shear
- non linearity of response is caused by continuous random breaking and formation of bonds
54
Shear thickening
Response of system is non linear
Corresponding rate decreases with stress resulting in an increase of viscosity
Dilatant behaviour
55
Causes for shear thickening
Changes inside a system which can lead to a viscosity increase:
- the spaces between particles tend to increase under shear resulting in voids
- particles become less lubricated after the voids are increased to a certain degree hence increased friction inside the system
- more interaction between particles due to disturbance of system
56
Time dependent behaviour
Viscoelastic materials may not adapt immediately to new shear conditions
57
Thixothrooy
Structure does not re form at the same speed and in the same way it is broken down
Can be seen for both shear thinning and thickening
58
Examples of plastic flow in pharmacy
Flocculated particles in conc disperse systems e.g. Ointments pastes creams
59
Pseudo-plastic flow in pharmacy examples
Natural synthetic and semi systemic polymers in solution e.g. Acacia, sodium alginate, methyl cellulose, hydroxylropylmethyl cellulose
60
Examples of dilatant flow in pharmacy
40-50% w/v suspensions of starch/water
61
Define flocculated particles
Internet
62
Can viscosity be measured at any point for non Newtonian fluids
No it cannot, it matter where it is measured and also how
63
What are capillary viscometers not capable of giving
Not capable of giving multiple points
64
Ideally which viscometers are used
Rheometers as falling sphere and simple rotational viscometer can be tedious
65
Rotational rheometers
Allow to employ a wide range of shear stress and rate
Small sample volume and good temp control
Allow continuous monitoring of structural changes in a sample over a range of stress, rate, time , temp
66
What are the different geometries
Parallel plate
Cone and plate
Mixer
Concenteric cylinder
67
Concentric cyclometer
For low viscosities or evaporating samples
68
Cone and plate
For viscous samples preferred for flow curves
69
Parallel plate
For samples containing particulates for oscillation and creep experiments
70
Mixer
In line viscosity control during manufacturing
71
Advantages of concentric cylinder
```
Little possibility of sample evaporation or expulsion
Can measure low shear stress which is useful for emulsions and suspensions
Easy to load with liquid dosage forms
n = T/kw
n = dynamic viscosity
T = torque (stress)
K = constant
w = speed of rotation
```
72
Disadvantages of concentric cylinder
Possible air incorporation or breaking of structure when loading semi solids
Large volume of material needed
Shear rate across gap in not constant varies with distance from wall. Can lead to slip or plug flow
73
Advantages of cone and plate
Cone has a very shallow angle of contact
Constant shear rate across radius
High shear rates possible
Small sample volume required
Easy to fill and clean even with highly viscous samples
Little disturbance of sample structure
Rapid temperature equilibration due to thin film
