Wm. Lu et al., EFFECTS OF BAFFLE DESIGN ON THE LIQUID-MIXING IN AN AERATED STIRRED-TANK WITH STANDARD RUSHTON TURBINE IMPELLERS, Chemical Engineering Science, 52(21-22), 1997, pp. 3843-3851
The effects of width and number of baffles in mechanically agitated ve
ssels with standard Rushton turbine impellers are examined for systems
with and without aeration. The insertion of the appropriate number of
baffles clearly improves the extent of liquid mixing. However, excess
ive baffling (i.e. n(b) >8 or B/T >0.2) and sparging gas through the i
mpeller would interrupt liquid mixing and lengthen the mixing time. Th
is study found that sparging gas through the impeller leads to an incr
ease in the mixing time of more than 20% because it reduces the liquid
pumping capacity of the impeller. A numerical technique was applied t
o examine the same effect on several extreme baffle conditions and the
cases of higher gas flow rates and rotational speeds. To generalize o
ur results obtained, the numerical technique was applied to simulate f
or a system with triple impellers. The trends of the mixing time were
found to be very similar to the single impeller system. By correlating
the mixing time with n(b), B/T, Q(g) and N, the following correlation
is obtained for the system with single Rushton turbine impeller under
non-gassed and aerated systems. Nt(M) = 55.7(n(b))(-0.30)(B/T)(-0.153
5)(Q(g)/ND3)(0.0296) and the similar correlation for the triple impell
er system can be given as Nt(M) = 46.5(n(b))(-0.295)(B/T)(-0.327)(Q(g)
/ND3)(0.010). (C) 1997 Elsevier Science Ltd.