Baffles
Number required for mixing and suspension
Ideal height of a tank in terms of its diameter for mixing
H = T
Ideal Clearance of the stirrer/impeller
C = T/3
Ideal shape of the base of a vessel
Dish based for optimum mixing
Axial Flow
Radial Flow
Static Volume
Liquid Volume beneath the impeller
~1% V
Minimum stirred Volume
Minimum mixed volume
Conical Tanks
Mixed flow impeller
Flow predominantly in axial direction with also a radial component
Close clearance impeller
Ensures good motion near vessel walls
Good for high viscous mixtures to facilitate heat transfer near the walls
Application of radial flow impellers
Applications of axial and mixed flow
Applications of close clearance impellers
- Blending
Baffles
- Tangential flow prevails in unbaffled tank (air entrainment, vortex formation and poor top-to-bottom mixing)
Controlling duty of processes
Importance of power dissipation
Aids for predicting:
mixing time, mass transfer coefficient, droplet size
Power Consumption Equation
P = 2piN*Lambda
N = Stirrer Rate Lambda = Torque
Impeller Power equation
P = Po roN^3 * D^5
Po = Power Number
Factors affecting Impeller power Number (Po)
Impeller Re Number
Re = roND^2/mu
N = impeller rotation rate
Power Curve Details
Blend Time Definition
Time to 95% homogeneity (Theta)