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A comparative study on effects of cone-plate and parallel-plate geometries on rheological properties under oscillatory shear flow

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The mathematical equations describing the viscoelastic properties corresponding to the PP and CP geometries are summarized in Table 1, where θ is the cone angle, T is the torque, Ω is the angular velocity, R is the radius of the plate and h is the size of the gap between the two plates while viscosity η is considered constant (Bohlin et al., 1980; Djalili-Moghaddam et al., 2004; Kavehpour and McKinley, 2004; Macosko, 1994). The subscript R in the equation for the cutting speed in the PP geometry indicates the edge cutting speed at the edge of the plate (radius R). They suggested that the generated nonuniform shear flow in the PP geometry produced higher viscosity than that of the CP geometry.

For strain-controlled LAOS tests (LAOStrain) (Ewoldt, 2013), typical strain sweep data are divided into linear and nonlinear regimes (Hyun et al., 2011). Many literatures show consistency of linear viscoelastic moduli between the two geometries and suggest that no correction is required in the linear regime, while mismatch occurs in the nonlinear regime (Bharadwaj and Ewoldt, 2015; de Souza Mendes et al., 2014 ; Shaw and Liu, 2006;. The horizontal displacement factor of 0.75 was used to compensate for the difference between two geometries, which is the ratio of the characteristic radius of the PP geometry to the total radius.

The same shift factor was obtained from the single-mode corotational Maxwell model (Giacomin et al., 2015). In this work, a general single-point correction was used to compensate for strain-controlled LAOS response measured by PP geometry. In general, oscillatory shear stress response under LAOS flow can be expressed by two types of equations (Hyun et al., 2011).

An alternative approach is to adjust the shear rate at the edge (radius R) to match a corresponding value in CP flow, which means horizontal shear (Giacomin et al., 2015; Wilhelm et al. derived the shear rate correction for shear-thinning effect-law fluids.

Fig. 1. Schematic views of torsional parallel-plate (PP) and cone-plate (CP) geometries for rheological  measurements
Fig. 1. Schematic views of torsional parallel-plate (PP) and cone-plate (CP) geometries for rheological measurements

Experimental

Single-phase system

  • Homopolymer melt and solution
  • Xanthan gum solution

Multiphase system

  • Polymer blend and nanocomposite
  • Suspension

Rheological measurements

Results and Discussion

SAOS data correction

Along with the single-phase systems, multiphase systems also show good agreement between CP and PP measurements, although PP/PS (80/20) blend shows small deviations between CP and PP measurements (Fig. 3a). But overall, no significant differences are observed in both single-phase and multi-phase systems when two geometries are compared. To compensate for residual differences between two geometries, PP data were shifted vertically to CP data using complex modulus, and the corresponding shift factors (VG*) are summarized in Table 2 .

Fig. 3. Comparison of linear viscoelastic properties of multi-phase systems at SAOS flow for parallel-
Fig. 3. Comparison of linear viscoelastic properties of multi-phase systems at SAOS flow for parallel-

LAOS data correction

In the linear regime, the first harmonic Fourier modulus (G′ and G″) from the CP and PP geometries overlap reasonably although the PP562T melt and the PP/PS blend (80/20) exhibit small deviations that may be caused by wall slip effects or gap placement problems (Egres and Wagner, 2005; . Shaw and Liu, 2006). In general, the PP geometry attenuates the first-harmonic nonlinearities (eg 4)) and leads to small overestimation of the first-harmonic Fourier modulus. Thus, all pre-harmonic nonlinearities measured by the PP must be vertically corrected to match the CP responses.

The validity of this vertical shift was verified experimentally for two first-harmonic intrinsic nonlinearities (𝐺31′ and 𝐺31′′) in the MAOS regime by using a correction factor of 1.5 predicted by a single-point correction (equation, however, for the other first-harmonic nonlinearities higher than the third order, such vertical shifts have not yet been reported.In addition, it is impossible to calculate the infinite number of first-harmonic nonlinearities from experiments. The associated shift factors (HG*) are summarized in Table 3, with vertical shift factors (VG*) to compensate for residual differences between CP and PP data.

Finally, we note that each power series expansion coefficient is corrected by the vertical displacement of the one-point correction, but the first harmonic Fourier module, which have complex relationships such as Eq. 4), are properly corrected for horizontal displacement. First harmonic modulus (G′ and G″) of PS2680 melts as a function of strain amplitude at 5 rad/s and 200°C for parallel plate (PP – filled symbols) and conical plate (CP – open symbols). The obtained vertical displacement factors (𝑉𝑄3) are listed in Table 3. The experimentally determined displacement factors are identical to the theoretical value of 1.5 within the measurement uncertainty, which agrees with the result of Giacomin et al. 2015) and reinforces the validity of the single point correction method.

A small amount of deviation can be explained by wall slip effects or gap placement problems (Egres and Wagner, 2005; Shaw and Liu derive differences of I3/1 between CP and PP measurements as functions of . It is speculated that the vertical displacement is sufficient for CP and PP data to be superimposed.Relative third harmonic intensity (I3/1) and nonlinear parameter (Q3) of PS2680 melts as a function of strain amplitude at 5 rad/s and 200°C for parallel plate (PP - filled symbols ) and cone plate (CP - open symbols) a), (c) Unshifted results and (b), (d) results shifted only according to the vertical shift factor.

In addition, Q5,0 parameter, an asymptotic value of Q5 at low strain amplitude, can be corrected by the value of 2 if the data exhibits a plateau behavior in the plot of Q5 as a function of strain amplitude. Relative fifth-harmonic intensity (I5/1) and nonlinear parameter (Q5) of PS300_20 solution as a function of strain amplitude at 6.3 rad/s and 25°C for parallel plate (PP – filled symbols) and cone plate (CP – open) symbols). a), (c) Non-shifted and (b), (d) shifted results by vertical shift factor only. Horizontal and vertical shift factors used in LAOS data from homopolymer melts and solution and multiphase systems.

Fig.  5.  Comparison  of  first-harmonic  Fourier  moduli  of  multiphase  systems  under  LAOS  flow  for
Fig. 5. Comparison of first-harmonic Fourier moduli of multiphase systems under LAOS flow for

Vertical and horizontal shifting in xanthan gum solutions

Since xanthan gum solutions exhibit shear thinning according to power law behavior, the theoretical shear rate correction factor was calculated by Eq. It is speculated that the horizontal shift in xanthan gum solutions is related to the approximation of the shear rate correction of Eq. Shear thinning index (n) of xanthan gum solution and corresponding shear rate correction factor calculated by Eq.

Stress response of 4 wt% xanthan gum solutions measured at CP (blue color) and PP (black color) at 1 rad/s and 25°C. Horizontal and vertical displacement factors used in first-harmonic Fourier moduli of xanthan gum solutions. Although a single vertical displacement factor of approx. 1.5 is able to superimpose I3/1 and Q3 measured at CP and PP for materials used in the previous section, the superposition is achieved by using a horizontal shift factor as well as a vertical shift factor, in the case of xanthan gum solutions.

Unlike the systems in the previous section, where the superposition of I3/1 and Q3 was obtained with only vertical shift factors, the horizontal shift factor has a dominant contribution to the I3/1 superposition of 0.5 wt. % xanthan gum solution. A solution of xanthan gum with a concentration of 4 wt. % also shows good agreement between CP and PP data with horizontal and vertical displacement factors, except for the voltage overshoot regime in Q3 (Figure 14). A difference between the overshoot peaks of CP and PP measurements is observed in xanthan gum solutions showing the LAOS type.

Relative third-harmonic intensity (I3/1) and nonlinear parameter (Q3) of 0.5 wt% xanthan gum solution as a function of strain amplitude at 1 rad/s and 25°C for the parallel plate (PP - symbols of filled) and the conical plate (CP – open symbols). a), (c) Unshifted and (b), (d) shifted results according to horizontal and vertical shift factors. Relative third-harmonic intensity (I3/1) and nonlinear parameter (Q3) of 4 wt% xanthan gum solution as a function of strain amplitude at 1 rad/s and 25°C for the parallel plate (PP - filled symbols) and the conical plate (CP – open symbols). a), (c) Unshifted and (b), (d) shifted results according to horizontal and vertical shift factors. LAOS Ⅰ-type xanthan gum solutions exhibit a perfect horizontal and vertical overlap of I5/1 and Q5.

However, the experimentally determined values ​​for all xanthan gum solutions average 2.11 for Q3 and 4.10 for Q5 (Table 6). Another possibility is an invalidity of a power series expression of nonlinear shear stress in xanthan gum solutions. That is, nonlinear shear stress of xanthan gum solutions may not be explained by power series expansion.

The relative intensity of the fifth harmonic (I5/1) and the nonlinear parameter (Q5) 4 mas. % xanthan gum solution as a function of strain amplitude at 1 rad/s and 25 °C for a parallel plate (PP – filled symbols) and a conical plate (CP – open symbols). a), (c) Unshifted and (b), (d) shifted results with horizontal and vertical shift factors. Horizontal and vertical displacement factors used in nonlinear parameterization of FT-based xanthan gum solutions.

Fig. 9. Non-shifted first-harmonic (a) storage and (b) loss moduli of xanthan gum solutions with 0.5, 1,
Fig. 9. Non-shifted first-harmonic (a) storage and (b) loss moduli of xanthan gum solutions with 0.5, 1,

Conclusion

This finding for xanthan gum solutions confirms the importance of shear rate correction in power law shear thinning or yield stress fluids. Grant Program (2014H1A2A1015767) and Basic Science Research Program (2015R1D1A1A09057413) through the National Research Foundation of Korea (NRF) funded by the Ministry of Education. FernÁndez, 2007, THE EFFECT OF TEMPERATURE, GEOMETRY, CUTTING AND SURFACE FRICTION ON THE FLUCTUATING RHEOLOGICAL PROPERTIES OF POTATO PORES, J.

Ewoldt, 2014, A simple thixotropic-viscoelastic constitutive model produces unique signatures in large amplitude oscillatory shear (LAOS), J. Wyss, 2014, A new approach to computing the true stress response from large amplitude oscillatory shear (LAOS) measurements using parallel plates, Rheol. Lee, 2003, Nonlinear response of complex fluids under LAOS (large amplitude oscillatory shear), Korea-Aust.

McKinley, 2011, A review of nonlinear oscillatory shear tests: Analysis and application of large amplitude oscillatory shear (LAOS), Prog.

Gambar

Fig. 1. Schematic views of torsional parallel-plate (PP) and cone-plate (CP) geometries for rheological  measurements
Table 1. Working equations for parallel-plate (PP) and cone-plate (CP) geometries.
Fig. 3. Comparison of linear viscoelastic properties of multi-phase systems at SAOS flow for parallel-
Table 2. Vertical shift factors used in SAOS data of single-phase and multiphase systems
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