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Of particular interest is the optimal fluid shear level needed to produce low turbidity water.
Image analysis has enabled to quantify the interfacial crack growth rate as a function of shear level.
At each shear level, the hydraulic pressure ranged from 0 to 0.6 MPa, and the normal load varied from 7 to 35 kN.
During the micro-scale fluidic transport as generated by moving members within active micro-devices and also owing to the interfacial shear level close to the surfaces in both active and passive micro-devices there is a general loss of viability of the transported sample.
However, the nature of base shear level variation suggests that this spectrum can be 'modified' to bring the base shear level in an acceptable range.
Again, the nature of base shear level variation suggests that this spectrum needs to be 'modified' for CHBDC incorporation to bring the base shear level in an acceptable range.
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Interestingly, COL1A1 expression was significantly lower compared to controls at all investigated shear levels (Fig. 3e).
High shear levels destroy the flocs and reduce dewaterability.
High floc settling velocities were correlated with low residual turbidities, both of which were optimized at low fluid shear levels and long fluid residence times.
A hydraulic tube flocculator was used to study how fluid shear levels affect the settling properties of a flocculated alum-kaolin suspension.
They are therefore useful when high and quickly adaptable oxygen supply is required, as they avoid also the presence of mechanically moving parts and present lower shear levels than mechanically stirred tanks.
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