EBB 220/3 POLYMER RHEOLOGY - PowerPoint PPT Presentation

1 / 46
About This Presentation
Title:

EBB 220/3 POLYMER RHEOLOGY

Description:

EBB 220/3 POLYMER RHEOLOGY Rheology = Science of deformation and flow of matter A very high performance polymer granules or pellets (raw materials) is useless if it ... – PowerPoint PPT presentation

Number of Views:878
Avg rating:3.0/5.0
Slides: 47
Provided by: material6
Category:

less

Transcript and Presenter's Notes

Title: EBB 220/3 POLYMER RHEOLOGY


1
EBB 220/3POLYMER RHEOLOGY
2
Introduction
  • Flow process in manufacturing polymer products
    can be represented as follows

3
Introduction
  • Rheology Science of deformation and flow of
    matter
  • A very high performance polymer granules or
    pellets (raw materials) is useless if it cannot
    be transformed into a practically useable
    products
  • Transformation means deformation and flow of
    polymer raw materials into a specified and
    required shapes
  • The rheology of polymer powder or pallet is
    importance in first section melts or liquids.

4
Introduction
  • In melt processing of thermoplastics polymers ?
    rheological studies give initial information on
    how these polymer behave during actual polymer
    processing.
  • e.g effect of temperature, pressure geometry
    on polymer flow behaviour in processes such as
    extrusion injection moulding
  • Flow behaviour is important in injection molding,
    compression moulding, blow moulding, calendering
    cold forming and spinning of fibres
  • It is also importance in the formulation of
    polymeric materials in preparing for fabrication
    process especially extrusion and mill rolling

5
  • For many simple fluids the study of rheology
    involves the measurement of viscosity ? the
    viscosity depends primarily on temperature and
    hydrostatic pressure
  • However the rheology of polymers is much more
    complex because the fluid shows non ideal
    behaviour

6
  • All these rheological properties depend upon the
    rate of shear, the molecular weight, structure of
    polymers the concentration of additives and
    temperature.
  • In most cases, flow is involved in the processing
    and fabrication of the plastics.

7
  • The degree of orientations is determined by
    rheological behaviour of the polymer and nature
    of the flow in fabrication process
  • Molecular orientation hence influence the
    mechanical properties of moulded object films and
    fibres

8
Importance of rheology
  • Mechanical properties that shown by any polymer
    products is the most importance factors
    considered by manufactured and user.
  • In actual conditions ? the optimum mechanical
    properties is not importance if the product could
    not be process as faster, simple or easier and
    relatively low cost
  • Flow involved is rheological studies that also
    involved
  • types and degree of orientation
  • Flow properties in actual processing

9
  • The importance of rheological studies are
  • Can identify the behaviour of flow during flowing
    together with factors that influenced the flow of
    polymers.
  • Can predict the real complex processing condition
    ? through easier component and predict the final
    properties of polymer
  • Can relate the qualitative and quantitative
    parameters such as output and used of materials
    properties

10
  • Can choose the suitable polymer for specific
    processing conditions and services
  • To produce a product with optimum processing
    properties.
  • ? importance in real processing to produce
    maximum output with minimum input
  • In some cases, factors as
  • Molecular structure,
  • morphology,
  • Polymer melt,
  • Blends and polymer modification
  • ? Can be studies by relationship between the
    rheological properties and materials structure.

11
Flow
  • Flow is the continuous deformation under an
    influenced of constant force
  • ? any particle of materials will not back to the
    original positions after the force of deformation
    been released
  • All the body in the nature will flow if given a
    period of time and appropriate temperature even
    with very low applied force

12
Flow
  • Ability to flow for a molten materials depends on
    the molecular chain mobility that hold molecule
    together.
  • Low mobility with high degree of chain
    entanglement ? will influenced the ability to
    flow and the process ability of polymeric
    materials

13
Example of flow
14
(No Transcript)
15
Viscosity
  • Consider 2 plates (A area of the plate),
  • separated by distance, D
  • The space between them is occupied by
  • the liquid
  • One plate moves relatively to the other
  • with velocity U
  • The movement is resisted by the viscous
  • reaction in the fluid
  • Since the movement is in shear, the
  • Reaction is the shear viscosity

F
A
S
?
D
Shear stress, ? Shear force/Area of the shear
face F/A Nm-2
Shear strain,? Amount of shear displacement,
S/Distance between shearing surfaces (D) Tan ?
Viscosity, ? Shear stress/Rate of shear strain
? / (d ?/dt)
? / ?
16
Viscosity
  • The unit of viscositiy was poise, P, or
    centipoise, cP.
  • 1 mPas 1 cP.
  • ? rapidly decreases as temperature increases.
  • Ideal fluids are called Newtonian. The viscosity
    is independent of the rate of shear

Shear rate is a measure of the rate of shear
deformation
Rheogram for Newtonian liquids. A - high
viscosity, B - low viscosity.
17
Newtonian Liquid
  • Newtonian liquid, where shear stress is
    proportional to shear rate, with the
    proportionality constant being the viscosity
  • A Newtonian fluid (named for Isaac Newton) is a
    fluid that flows like water
  • For example, water is Newtonian, because it
    continues to exemplify fluid properties no matter
    how fast it is stirred or mixed.
  • If the liquid is not Newtonian, a plot of shear
    vs. the rate of shear is not a straight line but
    a curve

18
Viscosity
  • - Most polymer melts rubber compound
  • behave in pseudoplastic.
  • How can we relate the pseudoplastic
  • behavior to the morphology of the polymer
  • (long chain coiled in complex structure)???
  • Dilatant behavior can cause processing
  • difficulties

Newtonian and non-Newtonian bahavior
Variation of apparent viscosity with shear rate
19
Viscosity
  • Thixotropy
  • Thixotropy is the property of some non-newtonian
    pseudoplastic fluids to show a time-dependent
    change in viscosity .
  • Viscosity decreases as the material is stirred
    until some minimum value is reached. It increases
    again when the substance is no longer agitated.
  • Many gels and colloids are thixotropic materials,
    exhibiting a stable form at rest but becoming
    fluid when agitated

Thixotropic substance at different shear rates.
20
Viscosity
  • When the relationship of shear stress t versus
    shear rate g is non-linear ? two types of
    viscosity at any value of shear rate can be
    obtained
  • Apparent viscosity ? from slope taken from a line
    that connect the value of shear stress with shear
    rate at any point of shear rate from the origin
  • Constant viscosity ? from slope taken from a line
    at particular value of shear rate for materials
    that showed non newtonian behaviour

21
Viscosity
  • When the curve is nonlinear, the viscosity
  • May be defined in two ways
  • Calculating apparent viscosity, ?a
  • Calculating consistency viscosity, ?c

?o viscosity at a very low shear Rate, which
behave like Newtonian behavior
?a is the slope of the secant line from the
origin to the shear stress at the given value of
shear rate
?c
?c the slope of the line at the chosen value
of Rate of shear
?o
?a
The ?a is greater than ?c
22
Non- newtonian flow
  • Most of the polymer systems not follow Newtonian
    law.
  • Non Newtonian flow can be classified into 3 parts
    as
  • Non time dependence flow,
  • Time dependence flow
  • Viscoelastic flow

23
Behaviour of viscous material
  • Materials will demonstrate behaviour
  • At low strain rate behave according to the
    Newtonian relationship
  • Totally dependent with time.
  • Stress being function of strain rate
  • Stress independent of strain

h viscosity de/dt strain rate
24
Non time dependence flow
  • Shear rate for non time dependence flow can
    represents mathematically the shear stress as
  • In rheological studies there are 4 types of flow
    that not dependence with time
  • Bingham body flow,
  • Pseudoplastic flow,
  • Newtonian flow
  • Dilatant flow

25
Shear rate Vs flow for non time dependence flow
26
(No Transcript)
27
Body Bingham flow
  • Body Bingham is elastic solid ? ideal materials
    that their structure will collapse when the
    stress applied greater than their yield stress
    ty,
  • Shear stress for body Bingham are proportional
    with shear rate given as
  • where h plastic viscosity that reach a infinity
    when shear rate almost zero (g? 0) and reach a
    value h when shear rate approach infinity value
    (g ? no limits).
  • Materials that represents model Bingham ?
    including emulsion and suspension with high
    concentration such as paint, printing ink, clay
    slurry and plastic emulsion.

28
Pseudoplastic flow
  • Viscosity of pseudoplastic flow decreased with
    the increased in shear rate ? it showed the shear
    thinning behaviour
  • During real processing that involved a higher
    range of shear rate ? no problems of flowing for
    pseudoplastic materials
  • At suppressed condition ? molecule has higher
    entanglement and will have random conformation or
    orientation
  • Under the applications of shear force ? uncoiled
    of molecule chain occur and the orientation of
    molecule increased even though the occurrence of
    Brownian movement will try to gives the original
    conformation (the condition where no force
    occurred)
  • At very high shear rate ? the almost Newtonian
    behaviour was observed for materials with
    pseudoplastic flows

29
Pseudoplastic
  • Pseudoplastic, or shear-thinning fluids have a
    lower apparent viscosity at higher shear rates.

Pseudo-plastic substance with yield value
Pseudo-plastic substance.
30
Newtonian Pseudoplastic Flow
31
Dilatant Flow
  • Viscosity value for Dilatant flow increased with
    increasing shear rate
  • ? its enable the polymer to be process at high
    shear rate due to the ability to flow polymer is
    low.
  • Dilatant behaviour normally shown by polymer with
    high suspension such as PVC and materials with
    non uniform particles shape ? ? materials that
    difficult to be compressed under high shear rate.
  • Dilatant behaviour is hardly shown for molten
    polymer except under a special condition ? where
    the melt crystallization occurred during flow.

32
Dilatant
  • A dilatant material is one in which viscosity
    increases with the rate of shear (also termed
    shear thickening).
  • The dilatant effect can be seen more readily with
    a mixture of corn starch and water

33
Time dependence flow
  • Flow properties that dependence with time are
    dependence on
  • Types of shear flow,
  • Flow history
  • Moulding time.
  • This types of flow showed a reversible conditions

34
Viscoelastic Flow
  • This flow are shown by materials that has the
    dominant viscous behaviour but has the elastic
    recovery after the deformation.
  • Viscoelastic flow has a properties in between the
    solid and liquid behaviour.
  • Please refer the viscoelastic behaviour
    (viscoelasticity)

35
Viscoelastic behaviour
  • Polymer is called viscoelastic because
  • Showing both behaviour elastic viscous
    behaviour
  • Instantaneously elastic strain followed by
    viscous time dependent strain

36
Influenced of temperature on viscosity
  • Understanding the influenced of temperature with
    the melt viscosity is importance in
  • Polymer processing
  • To estimate the thermal resistance of particular
    materials
  • Big variation in viscosity with range of
    temperature ? represent the materials need a
    higher activation energy
  • polymer molten viscosity that dependence on
    temperature have a higher temperature from glass
    transition temperature Tg or their melting
    temperature Tm.

37
  • The Andrade or Arrhenius equations can relate the
    activation energy during chain mobility as
  • Where h viscosity of polymer melt
  • AEa activation energy
  • R Universal gas constant
  • T Temperature (K)
  • A Arrhenius constant

38
  • When taking the logarithm plot from log h against
    log (1/T) ?will given one straight line where
    the slope is the same? activation energy
    according to this equations
  • If viscosity at various temperature taken at
    constant shear stress ? activation energy is
    supposed to be constant and not dependence on
    shear stress where it been taken.
  • If the viscosity at constant temperature at
    various shear rate ? activation energy dependence
    on shear rate
  • ? example activation energy decreased with
    increasing shear rate
  • However the flow according to Arrhenius
    equations? activation energy almost not
    dependence on temperature.

39
Instruments for rheology measurements
  • A very popular types of instruments to measure
    viscosity is capillary rheometer or viscometer
  • It function in conditions of load and forced is
    constant or at constant volume rate
  • In conditions of constant shear stress ?
    measurement of flow rate was taken based on the
    speed of piston
  • Pressure at the outer layer of die ? is measured
    using the pressure transducer

40
Viscometers
  • are employed to measure viscosity.
  • Capillary viscometer
  • Rotational rheometer
  • Simple shear viscometer
  • Cone plate rheometer
  • Parallel plate viscometer
  • Tensile extensional viscometer

Schematic diagram of a cone and plate viscometer.
Schematic diagram of a rotational viscometer
41
Instruments for viscosity measurements
Piston
Polymer melt
Barrel
Constant shear rate Rheometer
Pressure Transducer
Atmosphere pressure
Extrudate
42
Example of flow
43
Flow phenomena Rod climbing extrudate swell
44
Example of exams question
  • What are the importance of rheological studies in
    polymer processing.
  • Discuss the non-newtonian behaviour of polymeric
    materials.
  • What are the influenced of pseudoplastic flow
    towards polymer processing?
  • Most polymers melt exhibit pseudoplastic
    characteristics under shear conditions. How these
    differ from those of Newtonian fluids

45
Students Activity
  • Discuss with the person next to you what you
    understand on the importance of rheology in
    polymer processing

46
(No Transcript)
Write a Comment
User Comments (0)
About PowerShow.com