A comparison of three different methods for measuring both normal stress differences of viscoelastic liquids in torsional rheometers

A novel pressure sensor plate (normal stress sensor (NSS) from RheoSense, Inc.) was adapted to an Advanced Rheometrics Expansion System rheometer in order to measure the radial pressure profile for a standard viscoelastic fluid, a poly(isobutylene) solution, during cone–plate and parallel-plate shea...

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Published in:Rheologica acta Vol. 48; no. 2; pp. 191 - 200
Main Authors: Alcoutlabi, Mataz, Baek, S. G., Magda, J. J., Shi, Xiangfu, Hutcheson, S. A., McKenna, G. B.
Format: Journal Article
Language:English
Published: Berlin/Heidelberg Springer-Verlag 01-03-2009
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Abstract A novel pressure sensor plate (normal stress sensor (NSS) from RheoSense, Inc.) was adapted to an Advanced Rheometrics Expansion System rheometer in order to measure the radial pressure profile for a standard viscoelastic fluid, a poly(isobutylene) solution, during cone–plate and parallel-plate shearing flows at room temperature. We observed in our previous experimental work that use of the NSS in cone-and-plate shearing flow is suitable for determining the first and second normal stress differences N 1 and N 2 of various complex fluids. This is true, in part, because the uniformity of the shear rate at small cone angles ensures the existence of a simple linear relationship between the pressure [i.e., the vertical diagonal component of the total stress tensor (Π 22 )] and the logarithm of the radial position r (Christiansen and coworkers, Magda et al.). However, both normal stress differences can also be calculated from the radial pressure distribution measured in parallel-plate torsional flows. This approach has rarely been attempted, perhaps because of the additional complication that the shear rate value increases linearly with radial position. In this work, three different methods are used to investigate N 1 and N 2 as a function of shear rate in steady shear flow. These methods are: (1) pressure distribution cone–plate (PDCP) method, (2) pressure distribution parallel-plate (PDPP) method, and (3) total force cone–plate parallel-plate (TFCPPP) method. Good agreement was obtained between N 1 and N 2 values obtained from the PDCP and PDPP methods. However, the measured N 1 values were 10–15% below the certified values for the standard poly(isobutylene) solution at higher shear rates. The TFCPPP method yielded N 1 values that were in better agreement with the certified values but gave positive N 2 values at most shear rates, in striking disagreement with published results for the standard poly(isobutylene) solution.
AbstractList A novel pressure sensor plate (normal stress sensor (NSS) from RheoSense, Inc.) was adapted to an Advanced Rheometrics Expansion System rheometer in order to measure the radial pressure profile for a standard viscoelastic fluid, a poly(isobutylene) solution, during cone–plate and parallel-plate shearing flows at room temperature. We observed in our previous experimental work that use of the NSS in cone-and-plate shearing flow is suitable for determining the first and second normal stress differences N1 and N2 of various complex fluids. This is true, in part, because the uniformity of the shear rate at small cone angles ensures the existence of a simple linear relationship between the pressure [i.e., the vertical diagonal component of the total stress tensor (Π22)] and the logarithm of the radial position r (Christiansen and coworkers, Magda et al.). However, both normal stress differences can also be calculated from the radial pressure distribution measured in parallel-plate torsional flows. This approach has rarely been attempted, perhaps because of the additional complication that the shear rate value increases linearly with radial position. In this work, three different methods are used to investigate N1 and N2 as a function of shear rate in steady shear flow. These methods are: (1) pressure distribution cone–plate (PDCP) method, (2) pressure distribution parallel-plate (PDPP) method, and (3) total force cone–plate parallel-plate (TFCPPP) method. Good agreement was obtained between N1 and N2 values obtained from the PDCP and PDPP methods. However, the measured N1 values were 10–15% below the certified values for the standard poly(isobutylene) solution at higher shear rates. The TFCPPP method yielded N1 values that were in better agreement with the certified values but gave positive N2 values at most shear rates, in striking disagreement with published results for the standard poly(isobutylene) solution.
A novel pressure sensor plate (normal stress sensor (NSS) from RheoSense, Inc.) was adapted to an Advanced Rheometrics Expansion System rheometer in order to measure the radial pressure profile for a standard viscoelastic fluid, a poly(isobutylene) solution, during cone–plate and parallel-plate shearing flows at room temperature. We observed in our previous experimental work that use of the NSS in cone-and-plate shearing flow is suitable for determining the first and second normal stress differences N 1 and N 2 of various complex fluids. This is true, in part, because the uniformity of the shear rate at small cone angles ensures the existence of a simple linear relationship between the pressure [i.e., the vertical diagonal component of the total stress tensor (Π 22 )] and the logarithm of the radial position r (Christiansen and coworkers, Magda et al.). However, both normal stress differences can also be calculated from the radial pressure distribution measured in parallel-plate torsional flows. This approach has rarely been attempted, perhaps because of the additional complication that the shear rate value increases linearly with radial position. In this work, three different methods are used to investigate N 1 and N 2 as a function of shear rate in steady shear flow. These methods are: (1) pressure distribution cone–plate (PDCP) method, (2) pressure distribution parallel-plate (PDPP) method, and (3) total force cone–plate parallel-plate (TFCPPP) method. Good agreement was obtained between N 1 and N 2 values obtained from the PDCP and PDPP methods. However, the measured N 1 values were 10–15% below the certified values for the standard poly(isobutylene) solution at higher shear rates. The TFCPPP method yielded N 1 values that were in better agreement with the certified values but gave positive N 2 values at most shear rates, in striking disagreement with published results for the standard poly(isobutylene) solution.
Author Baek, S. G.
Magda, J. J.
McKenna, G. B.
Hutcheson, S. A.
Shi, Xiangfu
Alcoutlabi, Mataz
Author_xml – sequence: 1
  givenname: Mataz
  surname: Alcoutlabi
  fullname: Alcoutlabi, Mataz
  organization: Department of Materials Science and Engineering, University of Utah
– sequence: 2
  givenname: S. G.
  surname: Baek
  fullname: Baek, S. G.
  organization: RheoSense Inc
– sequence: 3
  givenname: J. J.
  surname: Magda
  fullname: Magda, J. J.
  email: jj.magda@m.cc.utah.edu
  organization: Department of Materials Science and Engineering, University of Utah
– sequence: 4
  givenname: Xiangfu
  surname: Shi
  fullname: Shi, Xiangfu
  organization: Department of Chemical Engineering, Texas Tech University
– sequence: 5
  givenname: S. A.
  surname: Hutcheson
  fullname: Hutcheson, S. A.
  organization: Department of Chemical Engineering, Texas Tech University
– sequence: 6
  givenname: G. B.
  surname: McKenna
  fullname: McKenna, G. B.
  organization: Department of Chemical Engineering, Texas Tech University
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Issue 2
Keywords Viscoelasticity
Normal stresses
Rheology
Pressure sensors
Viscoelastic fluid
Liquids
Shear flow
Measuring methods
Experimental study
Normal stress
Cone plate viscosimeter
Rheometer
Parallel plate
Rheological properties
Language English
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PublicationTitle Rheologica acta
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Snippet A novel pressure sensor plate (normal stress sensor (NSS) from RheoSense, Inc.) was adapted to an Advanced Rheometrics Expansion System rheometer in order to...
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SubjectTerms Characterization and Evaluation of Materials
Chemistry and Materials Science
Complex Fluids and Microfluidics
Cross-disciplinary physics: materials science; rheology
Exact sciences and technology
Fluid dynamics
Food Science
Fundamental areas of phenomenology (including applications)
Materials Science
Measurement methods
Mechanical Engineering
Methods
Non-newtonian fluid flows
Normal stress
Original Contribution
Physics
Polymer Sciences
Pressure distribution
Pressure sensors
Rheological measurements
Rheology
Rheometers
Shear flow
Shear rate
Shearing
Soft and Granular Matter
Stress concentration
Techniques and apparatus
Tensors
Torsion
Viscoelastic fluids
Viscoelastic liquids
Viscoelasticity
Title A comparison of three different methods for measuring both normal stress differences of viscoelastic liquids in torsional rheometers
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