L5/6- Agitation & mixing Flashcards

1
Q

Agitation

A

Induced motion of a fluid in a specified way (homogeneous material can be agitated)

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2
Q

Why Agitate?

A

Ensures contents are uniform in temp & composition;
Improves heat transfer between contents and wall/coil;
Speed up dissolving solid
Improve mass transfer
Suspend solids in solution

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3
Q

Mixing

A

Distribution of one initially separate phase into another (initially inhomogeneous phase only mixed)

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4
Q

Impeller Choices

A

Axial flow impellers or radial flow impellers

Propeller- (high speed axial flow) produces highly turbulent liquid & effective in bulk flow scenarios

Paddle- (simple flat paddle) no axial motion - radial and tangental, with up/downward motion at wall

Turbine- high speed rotation induces strong current in low viscosity systems

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5
Q

High speed Impellers for bulk fluid mixing

A

Propeller and pitched-bladed turbines

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6
Q

Low Speed agitators for viscous fluids

A

Paddle, anchor agitator, helical ribbon agitator

Prevents deposits on HT surface

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7
Q

Rushton turbine

A

Radial flow mixing- suitable for turblent flow also

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8
Q

Agitation Selection

A

Typically turbines except for high viscosity

Propeller for low viscosity

Angle blade turbine or axial flow propeller for keeping solids in suspension

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9
Q

Flow patters in mixing

A

Radial and longitudinal - provide flow for mixing

Tangential flow - suppresses flow by creating vortexes

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10
Q

Preventing swirl

A

Baffles to impede tangential motion without interfering with radial/longitudinal flows

Mounting impeller off centre

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11
Q

What happens if no baffles are present?

A

Overtopping as fluid rotates as solid body

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12
Q

Standard turbine - define variables

A

Da - agitator diameter
Dt - tank diameter
H - height of liquid
J - depth of baffle
E = height of centre-line of agitator
W = width/depth of agitator
L = length of agitator blade

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13
Q

Power number

A

Po = P/[(Da^5)(N^3)p]

Analagous to grag coefficient.

Proportional to ratio of drag force acting in unit area of impeller and inertial stress (flow of momentum of bulk motion)

Constant for high Re

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14
Q

Reynolds Number

A

Re = [(Da^2)Np]/mu

Proportional to diameter and peripheral speed of impeller

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15
Q

Froude Number

A

Fr = [(N^2)*Da]/g

Ratio of inertial stress to gravitational force per unit area acting on fluid

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16
Q

Rotator tip speed

A

Vtip = PIND

17
Q

Turbine impellers See lecture figure of 6 impellers

A

1) Flat six-blade disk turbine
2) Flat six blade open turbine
3) Six blade open tubrine at 450
4) Six-blade open turbine
5) Pitched curve blade turbine
6) Pitched blade turbine

2 and 4 only differ by blade depth- use for flat blade

18
Q

Critical Re number

A

Re c = [6370/Po^(1/3)]

For mixing to take place, flow must be fully turbulent, i.e. Re > Re c

19
Q

t95 parameter

A

Extent of mixing - time in seconds required for deviations from mean temp, conc. etc to be no more than 5% of the mean, starting with a fully stratified situation

Fo = [mut95]/[p(Dt^2)]

20
Q

Fourier Number

A

(Po^(1/3))ReFo = 5.2

21
Q

Mixing regimes

A

Different length and time scales of dominating mechanisms:

Macro, micro, meso

22
Q

Macromixing

A

Relates to scale of equipment (mm to m)

23
Q

Micromixing

A

Relates to size of smallest turblent eddies (micro m)

Length scale- smallest which flow has turbulent characteristics

24
Q

Mesomixing

A

In between macro and micro mixing

25
Q

Problems in micromixing

A

Local inhomogeneity on length-scale

26
Q

Kolmogoroff Microscale

A

/\k = [(v^3)/E]^(1/4)

27
Q

Lifetime of eddy, tow k

A

tow k = 12*[v/E]^(1/2)

Note E here is epsilon

28
Q

Engulfment rate, E

A

E = ln2/tow k

29
Q

Rate of engulfment, tow E

A

tow E = 1/E

30
Q

What ratio is wanted to avoid problems of selectivity in micromixing?

A

tow R > tow E

Avoid problem of selectivity determined by micromixing rather than intrinsic kinetics

31
Q

Kinematic viscosity

A

v = (mu/p)