How to extract the Newtonian viscosity from capillary breakup measurements in a filament rheometer

By G. H. McKinley, A. Tripathi. 2000

417 citations recorded by the source corpus.

Subfields: Electrical and Electronic Engineering, Fluid Flow and Transfer Processes, Polymers and Plastics

View Paper: https://www.semanticscholar.org/paper/a409054755aff73b13bc451cfefb7f3f45862cb0

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In Electrical and Electronic Engineering

In Fluid Flow and Transfer Processes

In Polymers and Plastics

Citations in the corpus

Microdevices for extensional rheometry of low viscosity elastic liquids: a review (2013, background): “187 188The relative merits of the CaBERTM and FiSERTM 189apparatuses, as well as the dynamics of capillary thinning 190of Newtonian and non-Newtonian fluids have been dis191cussed thoroughly by McKinley and Tripathi (2000), 192McKinley and Sridhar (2002) and McKinley (2005).”
Microfluidic extensional rheometry using a hyperbolic contraction geometry (2013, methodology): “The relaxation times of the PEO solution and DayQuil were measured using a capillary break-up extensional rheometer (CaBER) (McKinley and Tripathi 2000).”
Extensional rheology of a shear-thickening cornstarch and water suspension (2010, background): “…the extensional rheology of the less-concentrated and less-viscous fluids (Anna and McKinley 2001; Bazilevsky et al. 1990; Clasen et al. 2006; Entov and Hinch 1997; Kojic et al. 2006; McKinley and Tripathi 2000; Plog et al. 2005; Rodd et al. 2005; Stelter et al. 2000; Yesilata et al. 2006).”
Elasto-capillary thinning and breakup of model elastic liquids (2001, neutral): “…devices have been developed to specifically make measurements of visco-elasto-capillary thinning ͓Bazilevsky et al. ͑1990͒; Kolte and Szabo ͑1999͒; McKinley and Tripathi ͑2000͒; Stelter et al. ͑2000͔͒, the filament breakup experiments performed in the present study were actually carried out…”
Capillary Break-up Rheometry of Low-Viscosity Elastic Fluids (2005, methodology): “Provided gravitational effects are not important (so that Rmid lcap), the evolution in the midpoint radius is given by McKinley and Tripathi [5]: (4) The characteristic viscous time scale for the break-up process is thus tv = 14.1 mR0/s.”