2011
DOI: 10.1016/j.jnnfm.2010.12.007
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Squeeze flow of a power-law fluid between non-parallel plates

J.D. Sherwood
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Cited by 17 publications
(15 citation statements)
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“…5 One can also consider the flow under a constant applied force rather than plate translation velocity or, for rheological measurements, a constant sample mass vs. constant contact area with the plates. The more practically relevant situation of the squeeze flow of a non-Newtonian fluid (e.g., power-law, 6 viscoplastic, yield stress fluids, 2 etc.)…”
Section: Introductionmentioning
confidence: 99%
“…5 One can also consider the flow under a constant applied force rather than plate translation velocity or, for rheological measurements, a constant sample mass vs. constant contact area with the plates. The more practically relevant situation of the squeeze flow of a non-Newtonian fluid (e.g., power-law, 6 viscoplastic, yield stress fluids, 2 etc.)…”
Section: Introductionmentioning
confidence: 99%
“…The minimum gap height used in these studies is h = 400µm, which represents the distance between the two nearest points on the bounding plates. All models in this work assume parallel surfaces; a detailed analysis of higher order effects due to non-parallel plates can be found, for example, in [32] for power-law fluids.…”
Section: Acknowledgmentsmentioning
confidence: 99%
“…However, in the evolution of modern engineering, the role of non-Newtonian squeeze-flow is vital. Numerous scholars have analysed the squeezing flow problem with various non-Newtonian fluid models [19][20][21][22][23][24][25]. Amongst of these non-Newtonian models, couple stress fluid model proposed by Stoke's [26] has been given considerable attention by various investigators in field of fluid mechanics.…”
Section: Introductionmentioning
confidence: 99%