Basic Agitated vessel
design
Dipak Babu
seminar
Mixing Agitation
Basic definitions
 Agitation :
 Induced motion of a
material in a specified
way ,usually in a
circulatory pattern inside
some sort of a container.
 Mixing :
 Random distribution into
and through one another
,of two or more initially
separate phases.
A simple example
Gas A Gas B
blending
Sample A Sample B
Same composition = Agitation
Rotating drum
Different compositions = Mixing
 Blending of two miscible liquids ( ethyl alcohol and water).
 Dissolving solids in liquid ( salt in water).
 liquid-liquid dispersion (dispersion of pigment in solvents ).
 Suspending of fine solid particles in a liquid ( catalytic
hydrogenation of a liquid).
 Agitation of the fluid to increase heat transfer between the
fluid and a coil or jacket in the vessel wall.
 dispersing a gas in a liquid as fine bubbles, such as oxygen from
air in a suspension of microorganisms for fermentation or for
the activated sludge process in waste treatment.
Where is it used….??
The basic design
Influencing factors for
achieving a needed amount
of mixture or quality of
mixing :
1) Dimensions of the liquid
content of the vessel.
2) Dimensions and
arrangement of the
impellers , baffles .
http://commons.wikimedia.org/wiki/File:A
gitated_vessel.svg
 The vessel shape .
 The type , size , position and speed of the impeller.
 Flow patterns.
 Vortex formation.
 Baffles.
 Power correlations.
Design factors
The vessel
Rounded to eliminate
sharp corners or
regions into which
fluid currents would
not penetrate .
Height of fluid =
diameter of the
vessel
http://commons.wikimedia.org/wiki/File
:Agitated_vessel.svg
“The impeller”
Based on
viscosity
Based on
flow pattern
impellers
Axial – flow
impellers
propellers
High
efficiency
impellers
Radial – flow
impellers
turbines
Types …..!!!
Vessel illuminated with a number of
thin light sheets with different colors.
www.bakker.org
Pitched blade turbine
Three blade marine propeller Straight blade turbine
Concave blade impeller
Disc turbine
Image source : www.fusionfluid.com
Double flight helical
ribbon impeller
Impeller location : 1/6 the liquid level from the bottom
Impeller speed : standard speeds are 37, 45, 56, 68, 84, 100, 125, 155, 190, and
320rpm.
Power requirements usually are not great enough to justify the use
of continuously adjustable steam turbine drives.
Impeller size : the ratio of diameters of impeller and vessel falls in the range,
d/D,=0.3-0.6.
Another rule is that a second impeller is needed when the liquid must travel more
than 4 ft before deflection.
 Depend upon :
 The type of the impeller
 The characteristics of the liquid(especially viscosity)
 The size and proportions of : 1) tanks
2) baffles
3) impeller
Flow patterns
Vr
Vt
Vl
http://www.dynamixinc.com/baffled-by-baffles
Vortex elimination
Small tank
http://www.dynamixinc.com/baffled-by-baffles
Angle with the
radius
http://www.dynamixinc.com/baffled-by-baffles
“Baffles”
http://www.dynamixinc.com/baffled-by-baffles
Power consumption
Pumping number
Power number
Reynolds number
Power correlations
A simple numerical
For a vessel containing 5000 gal of liquid with specific gravity = 0.9
and viscosity of lOOcP, find size and speed of a pitched turbine
impeller to deliver 2 hp/1000 gal. Check also the superficial linear
velocity
Solution :
1) Size : d = 0.40 = 0.4(9.5)(12) = 45.6 in , say 46 in .
2) P= 2V = 2(5) = lO hp. (1 hp = 0.74 kW) = 7.4 kW .
Standard
speeds
Developed
formulae
Formulae source : www.pacontrol.com
Above 1000
1.3
N = 84 Rotations per minute
I fps = .308 m/sec
So 0.68 fps = 0.207 m/sec
1 cubic foot per second = 0.0283168466
cubic meters / second
48.1 cfs = 1.362 cubic meters / second
Input
parameters
www.checalc.com
identical
identical
www.checalc.com
 The performance of a particular agitator usually
cannot be predicted quantitatively.
 Agitator design is largely in exercise of judgment so
a considerable variety has been put forth by various
manufacturers.
 Developing software .
Conclusion
 www.fusionfluid.com
 www.checalc.com
 www.wikipedia.org
 www.bakker.org
 www.pacontrol.org
 www.safaribooks.org
 Unit Operations of Chemical Engineering (7th
edition)(McGraw Hill Chemical Engineering
Series)Warren McCabe Julian Smith Peter Harriott
 www.dynamixinc.com
Bibliography
Agitated vessel Design

Agitated vessel Design

  • 1.
  • 2.
  • 3.
    Basic definitions  Agitation:  Induced motion of a material in a specified way ,usually in a circulatory pattern inside some sort of a container.  Mixing :  Random distribution into and through one another ,of two or more initially separate phases.
  • 4.
    A simple example GasA Gas B blending Sample A Sample B Same composition = Agitation
  • 5.
  • 7.
     Blending oftwo miscible liquids ( ethyl alcohol and water).  Dissolving solids in liquid ( salt in water).  liquid-liquid dispersion (dispersion of pigment in solvents ).  Suspending of fine solid particles in a liquid ( catalytic hydrogenation of a liquid).  Agitation of the fluid to increase heat transfer between the fluid and a coil or jacket in the vessel wall.  dispersing a gas in a liquid as fine bubbles, such as oxygen from air in a suspension of microorganisms for fermentation or for the activated sludge process in waste treatment. Where is it used….??
  • 8.
    The basic design Influencingfactors for achieving a needed amount of mixture or quality of mixing : 1) Dimensions of the liquid content of the vessel. 2) Dimensions and arrangement of the impellers , baffles . http://commons.wikimedia.org/wiki/File:A gitated_vessel.svg
  • 9.
     The vesselshape .  The type , size , position and speed of the impeller.  Flow patterns.  Vortex formation.  Baffles.  Power correlations. Design factors
  • 10.
    The vessel Rounded toeliminate sharp corners or regions into which fluid currents would not penetrate . Height of fluid = diameter of the vessel http://commons.wikimedia.org/wiki/File :Agitated_vessel.svg
  • 12.
  • 13.
    Based on viscosity Based on flowpattern impellers Axial – flow impellers propellers High efficiency impellers Radial – flow impellers turbines Types …..!!!
  • 15.
    Vessel illuminated witha number of thin light sheets with different colors. www.bakker.org
  • 16.
    Pitched blade turbine Threeblade marine propeller Straight blade turbine Concave blade impeller Disc turbine
  • 17.
    Image source :www.fusionfluid.com Double flight helical ribbon impeller
  • 18.
    Impeller location :1/6 the liquid level from the bottom Impeller speed : standard speeds are 37, 45, 56, 68, 84, 100, 125, 155, 190, and 320rpm. Power requirements usually are not great enough to justify the use of continuously adjustable steam turbine drives. Impeller size : the ratio of diameters of impeller and vessel falls in the range, d/D,=0.3-0.6. Another rule is that a second impeller is needed when the liquid must travel more than 4 ft before deflection.
  • 19.
     Depend upon:  The type of the impeller  The characteristics of the liquid(especially viscosity)  The size and proportions of : 1) tanks 2) baffles 3) impeller Flow patterns
  • 20.
  • 21.
  • 22.
  • 23.
  • 24.
  • 25.
  • 26.
    Power consumption Pumping number Powernumber Reynolds number Power correlations
  • 29.
    A simple numerical Fora vessel containing 5000 gal of liquid with specific gravity = 0.9 and viscosity of lOOcP, find size and speed of a pitched turbine impeller to deliver 2 hp/1000 gal. Check also the superficial linear velocity Solution : 1) Size : d = 0.40 = 0.4(9.5)(12) = 45.6 in , say 46 in . 2) P= 2V = 2(5) = lO hp. (1 hp = 0.74 kW) = 7.4 kW .
  • 30.
  • 31.
  • 32.
    N = 84Rotations per minute
  • 33.
    I fps =.308 m/sec So 0.68 fps = 0.207 m/sec 1 cubic foot per second = 0.0283168466 cubic meters / second 48.1 cfs = 1.362 cubic meters / second
  • 34.
  • 35.
  • 36.
     The performanceof a particular agitator usually cannot be predicted quantitatively.  Agitator design is largely in exercise of judgment so a considerable variety has been put forth by various manufacturers.  Developing software . Conclusion
  • 37.
     www.fusionfluid.com  www.checalc.com www.wikipedia.org  www.bakker.org  www.pacontrol.org  www.safaribooks.org  Unit Operations of Chemical Engineering (7th edition)(McGraw Hill Chemical Engineering Series)Warren McCabe Julian Smith Peter Harriott  www.dynamixinc.com Bibliography

Editor's Notes

  • #9 But we do not have a cooling jacket … cause regulating a temperature may not be that important .. Check with upstream.
  • #15 See what they have in upstream
  • #26 Give a normal example as a blender