1983
DOI: 10.1007/bf01332368
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On nonlinear effects in the extensional flow of polymeric liquids

Abstract: The problems of uniform extension of liquids under constant strain rate and constant stretching force have been studied using a nonlinear rheological theory that describes the effects of finite elastic strains in viscoelastic liquids, with provision for the influence of deformative orientation on a scalar relaxation time. It has been shown that the predictions of the theory are in rather good agreement with numerous data for the extensional flow of polyisobutylene, even without taking the deformative orientati… Show more

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Cited by 34 publications
(10 citation statements)
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“…(26) agrees completely with the case of homogeneous extension at given constant force considered in [11]; this was the main reason for introducing the variables (23).…”
Section: E = X 2 -X -I + V ( Y 2 -Y -L )supporting
confidence: 65%
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“…(26) agrees completely with the case of homogeneous extension at given constant force considered in [11]; this was the main reason for introducing the variables (23).…”
Section: E = X 2 -X -I + V ( Y 2 -Y -L )supporting
confidence: 65%
“…Proposed in such a way this problem coincides exactly with that considered in [11] for the homogeneous…”
Section: ~(T) = [E(t)] -1/2 ~(T) _ ~ E(t') Dt'supporting
confidence: 51%
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“…For the purpose of the study we employ the slightly inhomogeneous approach [29] with the assumption that the averaged description of the cross-section variation of the extrudate is approximately true beginning with the outlet of the capillary die, as supposed in [30]. Since the extrudate is free from stresses (its total axial force is equal to zero), we have…”
Section: Distortions On the Extrudate Surface Due To Shear Oscillatiomentioning
confidence: 99%
“…The Leonov constitutive Equation (CE) and its variations have been successfully employed to model different types of flows including oscillatory shear, stress relaxation, steady shear, uniaxial extension, biaxial extension, startup shear, entrance flow, planar flow, and squeezing flow for both unfilled 28,29,38–65 and particle‐filled systems 28,29,37,66–74 . It has even been successfully employed to model the complex flow behavior encountered in injection molding for unfilled polymers 75,76 …”
Section: Leonov Constitutive Equationmentioning
confidence: 99%