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Oscillating shear capillary rheometry (OSCAR) for polymer melts

  • Dario Nichetti ORCID logo EMAIL logo
Published/Copyright: November 12, 2019
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Abstract

Knowing the flow parameters of a polymer melt under steady state condition is required to assess the performance of the material in die and mold design. Often, however, this is not sufficient for a full understanding of the polymer processing behavior, and information on the linear and non-linear viscoelastic behavior is needed. In this paper, the non-linear viscoelastic behavior of a polymer under shear flow has been investigated by measuring the stress response when a cyclic oscillating shear rate in a capillary rheometer is applied. The time-dependent wall shear stress has been decomposed into in-phase viscous and elastic components. A model to interpret the experimental results is presented and applied to a well-characterized polystyrene and two polyethylenes with similar rheology but different molecular structure (HDPE and LLDPE). The relevant characteristics resulting from the model, such as the generalized elastic and viscous modulus under shear, are compared and discussed.

References

[1] Bird RB, Armstrong RC, Hassager O. Dynamics of Polymeric Liquids, vol 1., Wiley: New York, 1987.Search in Google Scholar

[2] Han CD. Rheology and Processing of Polymeric Materials, Oxford University Press: New York, 2007.10.1093/oso/9780195187823.001.0001Search in Google Scholar

[3] Xie F, Halley PJ, Avérous L. Prog. Polym. Sci. 2012, 37, 595–623.10.1016/j.progpolymsci.2011.07.002Search in Google Scholar

[4] Housmans JW, Gahleitner MC, Peters GWM, Meijer HEH. Polymer 2009, 50, 2304–2319.10.1016/j.polymer.2009.02.050Search in Google Scholar

[5] Carneiro OS, Maia JM. Polym. Composites 2000, 21, 960–969.10.1002/pc.10249Search in Google Scholar

[6] Grizzuti N, Buonocore G, Iorio G. J. Rheol. 2000, 44, 149–164.10.1122/1.551073Search in Google Scholar

[7] Thomas DP, Hagan RS. Polym. Eng. Sci. 1969, 9, 164–171.10.1002/pen.760090304Search in Google Scholar

[8] Mitsoulis E, Delgadillo-Velazquez O, Hatzikiriakos SG. J. Non-Newton. Fluid Mech. 2007, 145, 102–108.10.1016/j.jnnfm.2007.05.004Search in Google Scholar

[9] Shaw MT. Introduction to Polymer Rheology, Wiley: New York, 2012.10.1002/9781118170229Search in Google Scholar

[10] Hatzikiriakos SG, Dealy JM. Polym. Eng. Sci. 1994, 34, 493.10.1002/pen.760340606Search in Google Scholar

[11] Bagley EB. J. Appl. Phys. 1957, 28, 624–627.10.1063/1.1722814Search in Google Scholar

[12] Mitsoulis E. J. Non-Newton. Fluid Mech. 1998, 78, 187–201.10.1016/S0377-0257(98)00073-1Search in Google Scholar

[13] Keslerová R, Trdlička D, Řezníček H. J. Phys. Conf. Ser. 2016, 38, 12112.10.1088/1742-6596/738/1/012112Search in Google Scholar

Received: 2019-07-19
Accepted: 2019-10-13
Published Online: 2019-11-12
Published in Print: 2020-10-25

©2019 Walter de Gruyter GmbH, Berlin/Boston

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