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The mixing rate of the particles is higher in the four-bladed mixer compared to the two-bladed mixer.
In general, measured conversions were higher with the static mixer, compared to an empty tube under mass-transfer limited conditions.
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A Roughton (R) style vortex mixer was compared to the more common impinging jet (IJ) mixer to assess differences in mixing performance.
Following this, for a Newtonian fluid, measurements of tangential velocity fluctuation obtained by Laser-Doppler Velocimeter (LDV) in an area located near the shaft of the mixer are compared to the computational fluid dynamic (CFD) values.
The mixers are compared to standard stirred vessels by Newton numbers.
It is found that the compressive strength and horizontal slump of mix obtained through Eirich mixer is higher compared to all other mixes.
Further, it may be deduced from Fig. 2 that the effect of pulsation intensity on mass transfer efficiency is more pronounced in the mixer-settler region compared to the effect for the region beyond the mixer-settler region (dispersion region).
Measured noise figure, conversion gain and compression point of the mixer are displayed and compared to the state of the art.
Drug loading obtained by coaxial turbulent jet mixer was higher than that reported for conventional bulk methods in literature, notwithstanding that NPs synthesized by coaxial turbulent jet mixer are much smaller compared to conventional bulk methods.
It is found that the Roughton mixer achieves a better mixing performance compared to the Y-mixer.
The mixing performance of the proposed vortex T-mixer with non-aligned inputs is compared to a simple T-mixer as a function of Reynolds number.
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