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Fibre spinning of a weakly elastic liquid
Institution:1. Department of Mathematics, University of British Columbia, Vancouver, BC V6T 1Z2, Canada;2. Department of Mechanical Engineering, Ohio University, Athens, OH 45701-2979, USA;1. John A. Paulson School of Engineering and Applied Sciences, Kavli Institute for Nanobio Science and Technology, Harvard University, Cambridge, MA 02138, United States;2. School of Aerospace Engineering and Applied Mechanics, Tongji University, Shanghai 200092, China;3. Department of Mechanical and Aerospace Engineering, University of California, Los Angeles, CA 90095, United States;1. Université de Nantes, CNRS, Laboratoire de Thermique et Energie de Nantes, UMR 6607, La Chantrerie, Rue Christian Pauc, B.P. 50609, Nantes Cedex 3 F-44306, France;2. Department of Organic Chemistry, University of Chemical Technology Prague, Technická 1905/5, Prague 166 28, Czech Republic;3. Institute of Macromolecular Chemistry Czech Academy of Sciences, Heyrovskeho nam. 2, Prague 162 06, Czech Republic;4. Laboratory of Technical Physics, School of Engineering, University of Liverpool, Liverpool, L69 3GH, United Kingdom;1. Department of Aerospace Engineering and Engineering Mechanics, University of Texas, Austin, TX, United States;2. Oden Institute for Computational Engineering and Science, University of Texas, Austin, TX, United States;3. School of Engineering and Applied Sciences, Harvard University, Cambridge, MA, United States
Abstract:This paper presents a study of a silicone oil (poly(dimethyl siloxane)) in extensional deformation using an instrument developed recently by the authors. Data from steady shear and low amplitude sinusoidal deformation of this liquid clearly establish that it is weakly elastic. The viscometric data, for shear rates less than 100 s −1, are best represented by either the Maxwell model or the Jeffrey's model, the latter being marginally superior. The extensional data show that at low deformation rates, this fluid exhibits a Newtonian behavior with an apparent extensional viscosity equal to three times the shear viscosity. Under these conditions the velocity profiles along the spinline are also well represented by the Newtonian model. However, at higher deformation rates better predictions of the velocity profiles are obtained from the Jeffrey's and Maxwell models. At deformation rates above 100 s −1 none of these simple models is adequate. Under the conditions used in these experiments, the fractional increase in tensile stress along the fiber is shown both theoretically and experimentally to be a unique function of the total strain. Furthermore, the apparent extensional viscosity at any point on the spinline can be calculated from steady state expressions if allowance is made for the variation of stretch rates by defining a time averaged stretch rate.The results obtained here show that elasticity must be considered if these model liquids are used to conduct rheological experiments at high deformation rates. Additionally, it is found that elastic effects in extension can be predicted using simple constitutive equations provided viscometric data can be represented properly in the deformation rate range of interest. Finally, the present research further substantiates the utility of the extensional viscometer developed by the authors.
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