2020
DOI: 10.1007/s42452-020-03561-w
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Measurement of the flow behavior index of Newtonian and shear-thinning fluids via analysis of the flow velocity characteristics in a mini-channel

Abstract: An in-situ measurement technique to determine the rheology of a fluid based on the experimentally measured velocity profile of a flow in a mini-channel is introduced. The velocity profiles of a Newtonian and different shear-thinning fluids along a rectangular channel were measured using shadowgraph particle image velocimetry (PIV). Deionized water and different concentrations of a polyacrylamide solution were used as Newtonian and shear-thinning fluids, respectively and were studied at different Reynolds numbe… Show more

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Cited by 54 publications
(21 citation statements)
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“…Higher viscosity and proper control printing at 210 • C with bed temperature of 60 • C were optimized for high dimensional accuracy between the successive of voids between the layers in the 3D printings [5]. The power-law model as presented in Equation ( 2) is determined the flow behavior to identify 3D printing layer and dimensional stability [11,31], where τ is shear stress, . γ is shear rate, K is consistency index, and n is power-law index, which were estimated by the power regression.…”
Section: Rheological Propertiesmentioning
confidence: 99%
“…Higher viscosity and proper control printing at 210 • C with bed temperature of 60 • C were optimized for high dimensional accuracy between the successive of voids between the layers in the 3D printings [5]. The power-law model as presented in Equation ( 2) is determined the flow behavior to identify 3D printing layer and dimensional stability [11,31], where τ is shear stress, . γ is shear rate, K is consistency index, and n is power-law index, which were estimated by the power regression.…”
Section: Rheological Propertiesmentioning
confidence: 99%
“…During 2 ml/min~4 ml/min, the Psd of CMC solution has the same trend as the Psd of water. When the shear-thinning fluid has a high shear rate, the fluid will enter a high-shear-rate viscosity plateau [22]. When the inlet flow rate is greater than 2 ml/min, the calculated fluid shear rate (8vL/d) reaches 8000~9000s -1 [23], consistent with the shear rate in the stable viscosity zone measured by the rheometer.…”
Section: Pressure Drop Of Single-phase Flowmentioning
confidence: 60%
“…When n reaches values beyond unity, the material is starts thinning upon the applied shearing force and when it exceeds the value of unity, the material starts shear thickening and reacts to the viscosity increase. In the first case, the lower the n value, the higher the deviation from Newtonian flow [ 48 ]. The K parameter, in turn, is described as the consistency coefficient and is equal to the shear stress at a shear rate of 1.0 s −1 .…”
Section: Resultsmentioning
confidence: 99%