2013
DOI: 10.1063/1.4802618
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Rheological evaluation of melt blown polymer melt

Abstract: Abstract. In this work, shear and uniaxial extensional viscosities of polypropylene melt blown sample with melt flow rate equal to 450 g/10min have been determined in wide deformation rate range by using capillary rheometry and novel orifice die design and the capability of recently proposed generalized Newtonian model to describe the measured experimental data has been tested.

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Cited by 3 publications
(1 citation statement)
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“…For the pure shear flow, the function f ( I |D| , II D , III D ) becomes equal to 1 and thus, the viscosity becomes a function of second invariant of deformation rate tensor D (IID=sans-serifγ˙2) only. In the pure uniaxial extensional flow, where I|D|= 2trueε˙, IID=3sans-serifε˙2, and IIID=sans-serifε˙3/4, the function f ( I |D| , II D , III D ) becomes nonzero and model becomes capable of representing steady-state extensional flows for different polymer melts [69,70,71,72,73,74].…”
Section: Theoreticalmentioning
confidence: 99%
“…For the pure shear flow, the function f ( I |D| , II D , III D ) becomes equal to 1 and thus, the viscosity becomes a function of second invariant of deformation rate tensor D (IID=sans-serifγ˙2) only. In the pure uniaxial extensional flow, where I|D|= 2trueε˙, IID=3sans-serifε˙2, and IIID=sans-serifε˙3/4, the function f ( I |D| , II D , III D ) becomes nonzero and model becomes capable of representing steady-state extensional flows for different polymer melts [69,70,71,72,73,74].…”
Section: Theoreticalmentioning
confidence: 99%