Presentación de PowerPoint - Nanbiosis · 2017. 12. 14. · Creep > 0 Recovery = 0 (after steady...

1
Creep > 0 Recovery = 0 (after steady state) Recoverable strain Introduction Rheology is the science that studies flow and deformation of materials under the effect of an applied force Flow Oscillation Creep and recovery Viscosity () is the resistance to flow. depends on shear rate. Creep: slow deformation of a material, usually measured under a constant stress. The creep test gives a measure of elastic, viscoelastic and viscous components. The compliance is defined as the ratio of the strain to the applied stress (J ). Oscillatory measurements are used to measure the viscoelastic properties of a material. A stress or strain is applied and the corresponding response (strain or stress) is measured. Ideal solids They flow. The energy is dissipated in the form of heat. The energy required for the deformation is fully recovered when the stresses are removed. reversibly Deform Ideal liquids irreversibly Geometries Rheology applications Yield stress Some samples require a certain stress to flow. Thixotropy Bingham (Newtonian with yield) Bingham Plastic (shear thinning with yield) Pseudo-plastic (shear thinning) Newtonian Dilatant (shear thickening) Shear rate (1/s) . Thixotropy is a time - dependent shear thinning property, which is used to characterize structure change reversibility. : stress (Pa) : shear rate (1/s) : Viscosity: (Pa·s) Storage Modulus G’ (Elastic parameter) Loss Modulus G” (Viscous parameter) tan = cos " = sin tan = " Complex Modulus G* A strain sweep is used to measure the linear viscoelastic region (LVR). From a strain sweep cohesive energy (CE) can be calculated to determine stability. The larger the cohesive energy the more stable is the sample. = + " G’ = References Ge l point : represents the point where behaviour changes from viscous (liquid- like) to elastic (solid-like). Quality control of polymers Improvement of the processing behaviour Optimization of the end product = 1 2 2 The greater the compliance the more the material can be strained under the application of a certain shear stress. (1) H.A. Barnes, J. F. Hutton, K. Walters F.R.S.,An Introduction to Rheology, Elsevier, Amsterdam, 1993. (2) F. Chambon, J. Winter, J. Rheol. 3 (8), 683-697, 1987. (3) www. tainstruments.com. Yield stress ( ) Stress Bingham (Newtonian with yield) Bingham Plastic (shear thinning with yield) Pseudo-plastic (shear thinning) Newtonian Dilatant (shear thickening) Shear rate (1/s) Viscosity (Pa·s) = Concentric cylinders Very low to medium viscosity Cone and plate Very low to high viscosity Parallel plates Low viscosity to soft solids Storage Transport Sedimentation Sagging Levelling Dipping Pouring Mixing Roller coating Spraying Extrusion Pumping Brushing High Low Viscosity 10 -6 1 10 6 Shear rate Deform at rest under shear Viscosity of different processes vs shear rate

Transcript of Presentación de PowerPoint - Nanbiosis · 2017. 12. 14. · Creep > 0 Recovery = 0 (after steady...

Page 1: Presentación de PowerPoint - Nanbiosis · 2017. 12. 14. · Creep > 0 Recovery = 0 (after steady state) Recoverable strain Introduction Rheology is the science that studies flow

Creep > 0 Recovery = 0 (after steady state)

Recoverable strain

IntroductionRheology is the science that studies flow and deformation of materials

under the effect of an applied force

Flow

Oscillation

Creep and recovery

Viscosity () is the “resistance to flow”.

depends on shear rate.

Creep: slow deformation of a material, usually

measured under a constant stress. The creep test

gives a measure of elastic, viscoelastic and viscous

components.

The compliance is defined as the ratio of the

strain to the applied stress (J ).

Oscillatory measurements are used to measure the viscoelastic properties of a material. A stress or strain is applied and

the corresponding response (strain or stress) is measured.

Ideal solids

They flow. The energy is dissipated in the form of heat.

The energy required for the deformation is fully recoveredwhen the stresses are removed.

reversiblyDeform

Ideal liquids irreversibly

Geometries

Rheologyapplications

Yield stress

Some samples require a certain

stress to flow.

Thixotropy

Bingham (Newtonian with yield)

Bingham Plastic (shear thinningwith yield)

Pseudo-plastic (shear thinning)

Newtonian

Dilatant (shear thickening)

Shear rate (1/s).

Thixotropy is a time-dependent shear thinningproperty, which is used to characterize structure change

reversibility.

: stress (Pa)

ሶ𝛾: shear rate (1/s)

: Viscosity: (Pa·s)

Storage Modulus G’(Elastic parameter)

Loss Modulus G”(Viscous parameter)

tan

𝐺′ = 𝐺∗ cos 𝛿

𝐺" = 𝐺∗ sin 𝛿

tan 𝛿 =𝐺"

𝐺′

Complex Modulus G*A strain sweep is used to measure the linear

viscoelastic region (LVR).

From a strain sweep cohesive energy (CE)can be calculated to determine stability.

The larger the cohesive energy

the more stable is the sample.

𝐺∗ = 𝐺′ + 𝑖𝐺"

G’

𝐽 =𝑆𝑡𝑒𝑎𝑑𝑦 𝑠𝑡𝑎𝑡𝑒 𝑟𝑒𝑐𝑜𝑣𝑒𝑟𝑎𝑏𝑙𝑒 𝑠𝑡𝑟𝑎𝑖𝑛

𝑠𝑡𝑟𝑒𝑠𝑠

References

Gel point : represents the point where

behaviour changes from viscous (liquid-

like) to elastic (solid-like).

Quality control of polymers

Improvement of the processing behaviour

Optimization of the end product

𝐶𝐸 =1

2𝐺′𝛾𝑐

2

The greater the compliance the more the

material can be strained under the application of

a certain shear stress.

(1) H.A. Barnes, J. F. Hutton, K. Walters F.R.S., An Introduction to Rheology, Elsevier, Amsterdam, 1993.

(2) F. Chambon, J. Winter, J. Rheol. 3 (8), 683-697, 1987.

(3) www. tainstruments.com.

Yie

lds

tre

ss

()

Stress

Bingham (Newtonian with yield)

Bingham Plastic (shear thinning with yield)Pseudo-plastic (shear thinning)

Newtonian

Dilatant (shear thickening)

Shear rate ሶ𝜸 (1/s)

Vis

co

sit

y

(Pa

·s)

=𝜎

ሶ𝛾

Concentric

cylinders

Very low to

medium viscosity

Cone and

plate

Very low to high

viscosity

Parallel

plates

Low viscosity to

soft solids

Storage Transport

SedimentationSagging

Levelling

DippingPouring Mixing

Roller coating

Spraying

ExtrusionPumpingBrushing

High

Low

Vis

cosi

ty

10-6 1 106

Shear rate

Deform

at rest under shear

Viscosity of different processes vs shear rate