2018
DOI: 10.1122/1.4998704
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Rheological behavior of human blood in uniaxial extensional flow

Abstract: We present an investigation of the rheological behavior of whole human blood under uniaxial extensional flow. For that purpose, capillary breakup experiments were carried out by combining the slow retraction method, high-speed imaging techniques and an immiscible oil bath. The use of the oil bath was aimed at reducing liquid loss by evaporation and to reduce light refraction effects, thus allowing the visualization of the blood cells during the filament thinning. Extensional relaxation times were measured for … Show more

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Cited by 24 publications
(33 citation statements)
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“…The viscometer had operated at a wider range of frequency from ω = 0.3 rad/s to ω = 700 rad/s [29]. The previous study indicated that the time constant of whole blood was obtained as λcv = 1.5-13.4 ms for shear flow [29], and λcv = 114-259 ms for extensional flow [30]. On the other hand, under periodic blood flow in the microfluidic system, Figure 6A-b showed the simple fluidic circuit model of the microfluidic system.…”
Section: Quantificative Comparison Of Viscoelasticty Obtained With Prmentioning
confidence: 99%
“…The viscometer had operated at a wider range of frequency from ω = 0.3 rad/s to ω = 700 rad/s [29]. The previous study indicated that the time constant of whole blood was obtained as λcv = 1.5-13.4 ms for shear flow [29], and λcv = 114-259 ms for extensional flow [30]. On the other hand, under periodic blood flow in the microfluidic system, Figure 6A-b showed the simple fluidic circuit model of the microfluidic system.…”
Section: Quantificative Comparison Of Viscoelasticty Obtained With Prmentioning
confidence: 99%
“…The idea of using viscosity distribution function as appears in (25) is due to the theoretical and experimental results of blood viscosity behavior that obtained by Cerny and Walawender [4] and Pontrelli [44] and many others [39][40][41][42][43][44][45][46][47][48][49][50][51][52][53][54] as appear in…”
Section: Newtonian Fluid =mentioning
confidence: 99%
“…The idea to use the non-Newtonian fluid was due to the fact that the Newtonian model does not give an appropriate response to many discrepancies observed in experiments. [35][36][37][38][39][40][41][42][43] In this section a solution for the non-Newtonian case ( = 2) will be examined alongside edge conditions (30) and the normalized condition (20b). By substituting = 2 into Equations (9) and (15), we get:…”
Section: Non-newtonian Fluid =mentioning
confidence: 99%
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