Abstract
Strain recovery after the cessation of shear was studied in model immiscible blends composed of polyisobutylene drops (10–30% by weight) in a polydimethylsiloxane matrix. Blends of viscosity ratio (viscosity of the drops relative to the matrix viscosity) ranging from 0.3 to 1.7 were studied. Most of the strain recovery was attributable to interfacial tension, and could be well-described by just two parameters: the ultimate recovery and a single retardation time. Both these parameters were found to increase with the capillary number of the drops prior to cessation of shear. For blends that had reached steady shear conditions, the ultimate recovery decreased with increasing viscosity ratio, whereas the retardation time increased with increasing viscosity ratio. The retardation time was well-predicted, but the ultimate recovery was over-predicted by a linear viscoelastic model developed previously by Vinckier et al. (Rheol Acta 38:65–72, 1999).
Similar content being viewed by others
References
Graebling D, Muller R, Palierne JF (1993a) Linear viscoelastic behavior of some incompatible polymer blends in the melt. Interpretation of data with a model of emulsion of viscoelastic liquids. Macromolecules 26:320–329
Graebling D, Muller R, Palierne JF (1993b) Linear viscoelasticity of incompatible polymer blends in the melt in relation with interfacial properties. J De Physique Iv 3:1525–1534
Graebling D, Benkira A, Gallot Y, Muller R (1994) Dynamic viscoelastic behavior of polymer blends in the melt—experimental results for PDMS/POE-DO, PS/PMMA and PS/PEMA blends. Eur Polymer J 30:301–308
Gramespacher H, Meissner J (1992) Melt elongation and recovery of polymer blends, morphology, and influence of interfacial tension. J Rheol 41:27–44
Gramespacher H, Meissner J (1995) Reversal of recovery direction during creep recovery of polymer blends. J Rheol 39:151–160
Jacobs U, Fahrländer M, Winterhalter J, Friedrich C (1999) Analysis of Palierne’s emulsion model in the case of viscoelastic interfacial properties. J Rheol 43:1497–1509
Kitade S, Ichikawa A, Imura N, Takahashi Y, Noda I (1997) Rheological properties and domain structures of immiscible polymer blends under steady and oscillatory shear flows. J Rheol 41:1039–1060
Maffettone PL, Minale M (1998) Equation of change for ellipsoidal drops in viscous flow. J Non-Newtonian Fluid Mech 78:227–241
Oldroyd JG (1953) The elastic and viscous properties of emulsions and suspensions. Proc Roy Soc Lon A218:122–132
Taylor GI (1934) The formation of emulsions in deformable fluids of flow. Proc Roy Soc Lon A 146:501–523
Tucker CL, Moldenaers P (2002) Microstructural evolution in polymer blends. Annu Rev Fluid Mech 34:177–210
Velankar S, Van Puyvelde P, Mewis J, Moldenaers P (2001) Effect of compatibilization on the breakup of polymeric drops in shear flow. J Rheol 45:1007–1019
Velankar S, Van Puyvelde P, Mewis J, Moldenaers P (2004) Steady-shear rheological properties of model compatibilized blends. J Rheol 48:725–744
Vinckier I, Mewis J, Moldenaers P (1996) Relationship between rheology and morphology of model blends in steady shear flow. J Rheol 40:613–632
Vinckier I, Moldenaers P, Mewis J (1999) Elastic Recovery of immiscible blends 1. Analysis after steady state shear flow. Rheol Acta 38:65–72
Acknowledgements
We are grateful to the University of Pittsburgh and the ACS Petroleum Research Fund (Grant #39931-G9) for supporting this research.
Author information
Authors and Affiliations
Corresponding author
Appendix
Appendix
Figure 6 shows a typical dynamic mechanical frequency sweep measurement for a blend with 10 wt% drops. Also shown is the G′ expected from the components (calculated using the Palierne model with the interfacial tension set to zero). The most obvious feature is the pronounced shoulder in the measured G′ of the blend that is entirely absent from the components. This shoulder has been attributed to the interfacial tension and its characteristics can be related to the size of the drops in the blends (Graebling et al. 1993a, 1994; Vinckier et al. 1996). Such frequency sweep data have been analyzed extensively in past publications (Graebling et al. 1993a, 1994; Vinckier et al. 1996; Kitade et al. 1997; Velankar et al. 2001). Here we will follow the analysis outlined by Velankar et al. (2004), which was specifically devised for the situations in which the shoulder in G′ is prominent and well-separated from any higher frequency relaxations. The G′ expected from the components was first subtracted from the measured G′ of the blend. The remainder, which may be regarded as the interfacial contribution to the G′, was fitted to a sum a few (up to 3) Maxwell modes:
Fits were performed using the free gnuplot software as described previously (Velankar et al. 2004). A sample fit has been shown in Fig. 6, and additional examples have been shown previously (Velankar et al. 2004). In all cases, the Maxwell mode corresponding to the shoulder in G′ was separated from any other modes by at least one decade in frequency. Thus, for all practical purposes, the shoulder can be captured by only one Maxwell mode. The corresponding relaxation time, multiplied by the shear rate prior to cessation of shear, yields the dimensionless relaxation time λ *F1 . Equation 8 is then used to obtain the Ca.
Rights and permissions
About this article
Cite this article
Wang, J., Velankar, S. Strain recovery of model immiscible blends without compatibilizer. Rheol Acta 45, 297–304 (2006). https://doi.org/10.1007/s00397-005-0037-3
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s00397-005-0037-3