Handbook of Industrial Mixing 2003
DOI: 10.1002/0471451452.ch10
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Solid–Liquid Mixing

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Cited by 63 publications
(62 citation statements)
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“…Shear mixing and ultrasonication processes are currently the common techniques that are widely used on particle/filler dispersion process [6, 7, 10, 11, 13-15, 27-30, 36-38]. In the shear mixing process, fluid shear force and impacts among clay-clay particles as well as impeller-clay particles owing to the agitation of impeller break up clay aggregates into fine particles [39]. The illustration of fluid flow in shear mixing can be seen in Fig.…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Shear mixing and ultrasonication processes are currently the common techniques that are widely used on particle/filler dispersion process [6, 7, 10, 11, 13-15, 27-30, 36-38]. In the shear mixing process, fluid shear force and impacts among clay-clay particles as well as impeller-clay particles owing to the agitation of impeller break up clay aggregates into fine particles [39]. The illustration of fluid flow in shear mixing can be seen in Fig.…”
Section: Introductionmentioning
confidence: 99%
“…This physical process can suspend and disperse clay particles to make a slurry. According to Atiemo-Obeng et al [39], there are six key points to achieve good wettability of solid-liquid mixing, which are operation methods, phases, properties of solid and liquid phases, unit operation, vessel geometry and mixing parameters. Shear mixing techniques have been employed to obtain homogenous clay dispersion or clay wettability [13,28,37] and good interfacial bonding between clay nanofillers and polymer matrices [40].…”
Section: Introductionmentioning
confidence: 99%
“…A crude assumption, often used in practice takes the free terminal settling velocity of the particle as a representative of its mean slip velocity. 26,27 Although the values yielded by the described methodology are likely to be much more realistic, it is currently difficult to be certain about the accuracy of these estimations given that information on particle rotation and turbulent velocity fluctuations (including whether in or out of phase) of the two phases is still missing.…”
Section: Eulerian Mapsmentioning
confidence: 99%
“…Since the cell free microcarriers did not settle, it was speculated that this phenomenon was associated with cell attachment to microcarriers and subsequent increase in particle density. The minimum agitation speed, Njs, needed to maintain microcarriers in suspension, was calculated according to Zwietering equation (Ibrahim and Nienow, 2004), using a value of S (Zwietering constant) of 4.8 (Atiemo-Obeng et al, 2004). Njs was calculated at 43.6 rpm, a value inline with our experimental data that 50 rpm was enough to fully suspend the empty microcarriers.…”
Section: The Effect Of Agitation Rate On Cell Growth In Submentioning
confidence: 99%