2001
DOI: 10.1016/s0301-9322(01)00011-8
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Investigation of three dimensional interstitial velocity, solids motion, and orientation in solid–liquid flow using particle tracking velocimetry

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Cited by 33 publications
(14 citation statements)
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“…Previous work relating to convective heat transfer coefficient measurement have suggested higher values than expected by a static fluid assumption (Balasubramaniam & Sastry, 1994a, 1994b, and studies on fluid interstitial velocity using Particle Tracking Velocimetry (Zitoun, Sastry, & Guezennec, 2001) have revealed the presence of significant interstitial motion even at Reynolds numbers as low as 9.4 and solids loading as high as 50%. Regardless of what situations actually occur, it is prudent to consider all scenarios in design of safe processes.…”
Section: Particle-more-conductive Casesmentioning
confidence: 95%
“…Previous work relating to convective heat transfer coefficient measurement have suggested higher values than expected by a static fluid assumption (Balasubramaniam & Sastry, 1994a, 1994b, and studies on fluid interstitial velocity using Particle Tracking Velocimetry (Zitoun, Sastry, & Guezennec, 2001) have revealed the presence of significant interstitial motion even at Reynolds numbers as low as 9.4 and solids loading as high as 50%. Regardless of what situations actually occur, it is prudent to consider all scenarios in design of safe processes.…”
Section: Particle-more-conductive Casesmentioning
confidence: 95%
“…Since PTV requires independent particles to be distinguishable, it is typically used in dilute flows, for instance, in articles Zitoun et al (2001) and Peurrung et al (1995). In fluidized beds, the local volume fraction is rapidly changing, and therefore, the flow may become momentarily too dense for regular PTV algorithms.…”
Section: Introductionmentioning
confidence: 99%
“…For the penetrated particles, deposition probability should be determined in order to evaluate Journal of Petroleum Engineering the plugging phenomena in the porous media caused by the precipitated asphaltene particles. In such systems, solidsto-tube diameter ratios are typically in the range of 0.1-0.3 [28,32]. In this range, according to the filtration theories, straining filtration is applied.…”
Section: Bundle Of Tubes Modelingmentioning
confidence: 99%
“…where is the exponential function, 0 is a constant dependent on ionic conditions [24], V is the flow mean velocity inside a tube known as interstitial velocity which is the superficial velocity divided by porosity [32], and V * is the minimum fluidization velocity that can be calculated by knowing the particle and fluid density [34]. It is obvious from (9) that higher flow velocities reduce the value of .…”
Section: Bundle Of Tubes Modelingmentioning
confidence: 99%