2010
DOI: 10.1016/j.jfoodeng.2010.03.011
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Monitoring liquid displacement of model and industrial fluids in pipes by in-line ultrasonic rheometry

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Cited by 41 publications
(18 citation statements)
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“…UIV and its derivatives have proved successful not only for blood flow measurements [28,29] but also for applications to hydrodynamics [30], to rheology [13,31] or to industrial situations involving optically opaque suspensions [32,33]. These velocimetry techniques rely upon the measurement of local displacements through cross-correlation of successive speckle signals received after successive pulses are sent through the scattering material.…”
Section: Acoustic Imaging In Suspensions Of Non-brownian Particlementioning
confidence: 99%
“…UIV and its derivatives have proved successful not only for blood flow measurements [28,29] but also for applications to hydrodynamics [30], to rheology [13,31] or to industrial situations involving optically opaque suspensions [32,33]. These velocimetry techniques rely upon the measurement of local displacements through cross-correlation of successive speckle signals received after successive pulses are sent through the scattering material.…”
Section: Acoustic Imaging In Suspensions Of Non-brownian Particlementioning
confidence: 99%
“…The delay line is a material optimised for beam forming that contains the near-field distance. This delay line is fixed ahead of the transducer and is flush with the pipe wall, thus making it possible to have the focal point (position where sound energy is highest) of the ultrasonic beam at the wall interface (see Wiklund et al, 2010;Kotzé and Haldenwang, 2011;Kotzé et al, 2012Kotzé et al, , 2013. Standard transducers with a central basic frequency of 2 and 4 MHz were chosen in order to obtain a good compromise between spatial resolution, which is due to their short wavelength, and penetration depth (less attenuation).…”
Section: Uvp+pd Experimental Setup and Methodologymentioning
confidence: 99%
“…It is based on the traditional tube viscometry concept where the shear rate is obtained from the measurements of the volumetric flow rate and the shear stress at the wall is obtained from simultaneous measurement of the pressure difference over a fixed distance. The UVP+PD method and similar methods for determining the rheological parameters of a suspension or emulsion are already known and are described in several publications (Wunderlich and Brunn 1999;Dogan et al, 2005;Pfund et al, 2006;Wiklund et al, 2007;Birkhofer et al, 2008;Wiklund and Stading, 2008;Fock et al, 2009;Wassell et al, 2010;Wiklund et al, 2010;Kotze et al, 2008Kotze et al, , 2012. The UVP+PD methodology allows measurements not possible with commercial off-line rheometers such as radial velocity profiles and yield stress directly in-line and under dynamic process conditions.…”
mentioning
confidence: 99%
“…Examples include e.g. studies of paper pulp up to a volume fraction of 7.7% (Wiklund et al 2006), industrial suspensions and foods (Wiklund and Stading 2008;Wiklund et al 2010). These types of flow are echogenic by nature, i.e.…”
Section: Miscellaneous Applicationsmentioning
confidence: 99%