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    largely due to the local regions generated by the interaction of
    flow domains from different blades in different branches. With
    increasing particle loading, the extent of uniformity in the
    suspended particle concentration also increased. In the case of
    a PBTD, two different circulation loops, one below and another
    above the impeller are established. Unlike this, in the FI, higher
    solidity practically breaks such loops and develops several net-
    works of zones which interact with each other. This also helps to
    keep the particles suspended while being transferred from one
    zone to another self-similar zone. More detailed experiments on
    tracking of particles between zones would help to quantify the
    residence time of particles in different zones and thereby
    characterize the energy distribution in the stirred reactor with
    such an impeller. Such details are being investigated and will be
    reported separately.
    In another set of experiments, the performance of FI for
    suspending solid glass particles was studied. The Pw variation for
    different glass particle suspension densities is shown in
    Figure 5A.While the nature of plots is similar to that of Figure 3,
    the value of Pw at similar impeller rotation speed is almost twice
    that of the suspension of particles with density 1069 kg/m3
    . This
    extent of difference is almost equivalent to the settling velocity of
    these particles in water, which is proportional to their densities.
    Onmeasuring the cloud height for suspension of glass particles, it
    was seen that the extent of lifting of the particles in the bulk
    increased with increasing suspension density. This implies that
    the increase in power consumption at higher suspension den-
    sities was indeed utilized in suspending particles. Visual
    ), the FI showed much lower powerobservations showed that at very low suspension density, the
    particles always remained in the lower half of the impeller. This
    was largely because the particles were seen to remain entrapped
    in the smaller mixing zones formed by the blades of fractal
    impeller. This observation was also seen for higher suspension
    density, but at lower impeller rotation speed (<100 rpm) the
    particles were seen to get aligned in a peculiar manner at the tank
    bottom, in two lines each connecting the diagonally opposite
    baffles. On increasing impeller speed, they eventually get sus-
    pended. This indicates that at lower N, the confluence of radial
    flow, tangential flow, and the presence of baffles makes the
    particles to assemble in a specific manner. At higher suspension
    density (5%), the particles were seen to get easily suspended,
    which is not very common largely because of the variation in the
    bulk property which helped the particles get suspended easily.
    Equation 1 was seen as valid even for the suspension of glass
    particles with the value of C1 = 5.5  107
    .
    The performance of suspending identical glass particles in a
    stirred tank using FI and PBTD(in a large tank having identicalT/H
    ratio10
    ) is shown in Figure 5B. The observations for three different
    solid concentrations can be summarized as follows: (i) at 1% solid
    concentration, PBTD (filled symbols) performs much better than
    FI (open symbols) in suspending particles even at very low impeller
    speed; (ii) at 3% and 5% solid concentration, the power required for
    lifting of particles with PBTDis relatively lower than that of FI.With
    glass particles, the terminal velocity being higher, while achieving
    complete suspension was possible at lower Pw, achieving uniform
    suspension needed relativelymuch higher power. (iii)With 5%solid
    fraction, the FI is efficient in suspending particles at higher
    concentrations; (iv) the trend in the efficiently suspending the
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