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Turbulence is the dominant mechanism for the T/3 impeller.
The A310 impeller consumes significantly less power at Njs than the PBT.
Open image in new window Fig. 1 Viscosity measuring apparatus 1 torque meter; 2 electronic coupling meter; 3 outer magnetic jar; 4 thermocouple; 5—stimpellermpeller.
The models were tested using experimental data for two impellers, a Lightnin A310 impeller and a 45° pitched-blade turbine.
For the T/2 impeller some combination of turbulence and mean flow is required.
The experimental parameters were varied within the ranges: pressure (0.1 – 1.4Mpa), impeller frequency (8.3 – 41.7 s−1), catalyst weight (3 – 30·10−3kg) and particle size (0.6 – 5.5·10.6m).
A full top-to-bottom circulation loop was found in the A310 impeller system at higher speeds.
The work was conducted in 0.15 m diameter vessel (T) with a 45° impeller of diameter D (=0.45T) in water.
The geometric configurations of the pump-mixer studied are: (a) an R320 curved blade impeller, with variable clearance from the tank bottom, and (b) a multiple impeller set-up produced by the addition of an upper A310 impeller.
We examined the performance of 8 impeller geometries with blade stagger or twist angles varying from 100° to 800° using computational methods.
The mixing times in ungassed, cold gassed, hot sparged and boiling systems agitated by a single CD-6 impeller are also reported.
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