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L-25
Cyclones
Air Pollution and Control
(Elective-I)
Cyclones
• Settling chambers discussed in previous
lecture are not effective in removing small
particles.
• Therefore, one needs a device that can
exert more force than gravity force on the
particles so that they can be removed from
the gas stream.
• Cyclones use centrifugal forces for
removing the fine particles. They are also
known as centrifugal or inertial separators.
Prof S S Jahagirdar, NKOCET

2
Cyclone

Prof S S Jahagirdar, NKOCET

3
Vortex core
Main
Vortex

Prof S S Jahagirdar, NKOCET

4
CYCLONE
Outlet
Inlet
Vortex
Finder
Cylinder

Cyclone
body

Cone

Dust
Discharger

Prof S S Jahagirdar, NKOCET

5
Prof S S Jahagirdar, NKOCET

6
Prof S S Jahagirdar, NKOCET

7
• The cyclone consists of a vertically placed
cylinder which has an inverted cone
attached to its base.
• The particulate laden gas stream enters
tangentially at the inlet point to the
cylinder.
• The velocity of this inlet gas stream is
then transformed into a confined vortex,
from which centrifugal forces tend to
drive the suspended particles to the walls
of the cyclone.
Prof S S Jahagirdar, NKOCET

8
• The vortex turns upward after reaching at
the bottom of the cylinder in a narrower
inner spiral.
• The clean gas is removed from a central
cylindrical opening at the top, while the
dust particles are collected at the bottom
in a storage hopper by gravity.

Prof S S Jahagirdar, NKOCET

9
How particles separated from gas?
• A high rate of spin
Spinning gas
Centrifugal force fling the dust particles to the walls of
cylinder and cone
The particle then slide down the wall and into the
storage hopper
The cleaned gas gradually spiral downward …
The downward cleaned gas gradually reversed its
downward and forms a smaller ascending spiral
A vortex finder tube extending downward into the
cylinder aids in directing the inner vortex out of the
device
Cyclone
Dimensions
D= Body diameter
H= Height of inlet
W= width of inlet
Lc= Length of cone
Lb= Length of body
S= Length of vortex finder
De= Diameter of exit
Dd= Diameter of dust outlet

Prof S S Jahagirdar, NKOCET

11
Effective turns

Prof S S Jahagirdar, NKOCET

12
Equation
for dp
Vi = Gas Velocity at inlet (m/s or ft/s)

Prof S S Jahagirdar, NKOCET

13
dp is the size of the smallest
particle that will be collected if
it starts at the inside edge of
the inlet duct.
Thus, in theory, all particles of
size dp or larger should be
collected with 100% efficiency.
Prof S S Jahagirdar, NKOCET

14
Equation for Cut Size diameter

Prof S S Jahagirdar, NKOCET

15
Standard Cyclone

Prof S S Jahagirdar, NKOCET

16
Standard
Cyclone

Prof S S Jahagirdar, NKOCET

17
Prof S S Jahagirdar, NKOCET

18
Equation of Cyclone
•Lapple then developed a general curve for
standard conventional cyclones to predict the
collection efficiency for any particle size.
• If the size distribution of particles is known,
the overall collection efficiency of a cyclone can
be predicted by using above graph.
•Theodore and DePaola (1980) have fitted an
algebraic equation to above graph, which makes
Lapple’s approach more precise and more
convenient for application to computers.
Prof S S Jahagirdar, NKOCET

19
Prof S S Jahagirdar, NKOCET

20
Equation for efficiency

X 100

in %
Prof S S Jahagirdar, NKOCET

21
Prof S S Jahagirdar, NKOCET

22
Advantages
i)
ii)
iii)
iv)
v)

low initial cost,
simple in construction and operation,
low pressure drop,
low maintenance requirements,
continuous disposal of solid particulate
matter, and
vi) use of any material in their construction
that can withstand the temperature and
pressure requirements.
Prof S S Jahagirdar, NKOCET

23
Disadvantages
i) low collection efficiency for
particles below 5 – 10 µ in diameter,
ii) severe abrasion problems can occur
during the striking of particles on the
walls of the cyclone, and
iii) a decrease in efficiency at low particulate
concentration.

Prof S S Jahagirdar, NKOCET

24
Operational problems
• i) Erosion: Heavy, hard, sharp edged
particles, in a high concentration, moving
at a high velocity in the cyclone,
continuously scrap against the wall and
can erode the metallic surface.

Prof S S Jahagirdar, NKOCET

25
• ii) Corrosion: If the cyclone is operating
below the condensation point, and if
reactive gases are present in the gas stream,
then corrosion problems can occur. Thus the
product should be kept above the dew point
or a stainless steel alloy should be used.
• iii) Build – up: A dust cake builds up on the
cyclone walls, especially around the vortex
finder, at the ends of any internal vanes, and
especially if the dust is hygroscopic. It can
be a severe problem.
Prof S S Jahagirdar, NKOCET

26
Applications of cyclones
i) For the control of gas borne particulate
matter in industrial operations such as
cement manufacture, food and beverage,
mineral processing and textile industries.
ii) To separate dust in the disintegration
operations, such as rock crushing, ore
handling and sand conditioning in industries.
iii) To recover catalyst dusts in the petroleum
industry.
iv) To reduce the fly ash emissions.
Prof S S Jahagirdar, NKOCET

27
• Applications
•
•
•
•
•
•
•
•
•
•

Power Plant
Textile industry (Cotton, Polyester)
Stone Crusher
Mineral Industry
Rubber Industry
Material Handling
Fly Ash
Lead Industry
Cement Industry
Steel Industry
Prof S S Jahagirdar, NKOCET

28
Objective Questions
Q1. In cyclone particulate separation takes place
because of ________________ force.
Q2. Cyclone separator has ___________ inlet.
Q3. In case of cyclone equation for effective turns
is given by _______________.
Q4. Cut size diameter in case of cyclone can be
computed by using equation _______________.
Q5. In case of a standard cyclone length of conical
part is given by ________________. (similar
questions on dimensions of cyclone)
Prof S S Jahagirdar, NKOCET

29
Theory Questions
Q1. Discuss with neat sketch working
principle of cyclone. Also list its
advantages and disadvantages.
Q2. write short notes on:1. Standard cyclone
2. Operational problems in cyclone.
30
Prof S S Jahagirdar, NKOCET
Prof S S Jahagirdar, NKOCET

31
Prof S S Jahagirdar, NKOCET

32

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L 25 and 26 final

  • 1. L-25 Cyclones Air Pollution and Control (Elective-I)
  • 2. Cyclones • Settling chambers discussed in previous lecture are not effective in removing small particles. • Therefore, one needs a device that can exert more force than gravity force on the particles so that they can be removed from the gas stream. • Cyclones use centrifugal forces for removing the fine particles. They are also known as centrifugal or inertial separators. Prof S S Jahagirdar, NKOCET 2
  • 3. Cyclone Prof S S Jahagirdar, NKOCET 3
  • 4. Vortex core Main Vortex Prof S S Jahagirdar, NKOCET 4
  • 6. Prof S S Jahagirdar, NKOCET 6
  • 7. Prof S S Jahagirdar, NKOCET 7
  • 8. • The cyclone consists of a vertically placed cylinder which has an inverted cone attached to its base. • The particulate laden gas stream enters tangentially at the inlet point to the cylinder. • The velocity of this inlet gas stream is then transformed into a confined vortex, from which centrifugal forces tend to drive the suspended particles to the walls of the cyclone. Prof S S Jahagirdar, NKOCET 8
  • 9. • The vortex turns upward after reaching at the bottom of the cylinder in a narrower inner spiral. • The clean gas is removed from a central cylindrical opening at the top, while the dust particles are collected at the bottom in a storage hopper by gravity. Prof S S Jahagirdar, NKOCET 9
  • 10. How particles separated from gas? • A high rate of spin Spinning gas Centrifugal force fling the dust particles to the walls of cylinder and cone The particle then slide down the wall and into the storage hopper The cleaned gas gradually spiral downward … The downward cleaned gas gradually reversed its downward and forms a smaller ascending spiral A vortex finder tube extending downward into the cylinder aids in directing the inner vortex out of the device
  • 11. Cyclone Dimensions D= Body diameter H= Height of inlet W= width of inlet Lc= Length of cone Lb= Length of body S= Length of vortex finder De= Diameter of exit Dd= Diameter of dust outlet Prof S S Jahagirdar, NKOCET 11
  • 12. Effective turns Prof S S Jahagirdar, NKOCET 12
  • 13. Equation for dp Vi = Gas Velocity at inlet (m/s or ft/s) Prof S S Jahagirdar, NKOCET 13
  • 14. dp is the size of the smallest particle that will be collected if it starts at the inside edge of the inlet duct. Thus, in theory, all particles of size dp or larger should be collected with 100% efficiency. Prof S S Jahagirdar, NKOCET 14
  • 15. Equation for Cut Size diameter Prof S S Jahagirdar, NKOCET 15
  • 16. Standard Cyclone Prof S S Jahagirdar, NKOCET 16
  • 17. Standard Cyclone Prof S S Jahagirdar, NKOCET 17
  • 18. Prof S S Jahagirdar, NKOCET 18
  • 19. Equation of Cyclone •Lapple then developed a general curve for standard conventional cyclones to predict the collection efficiency for any particle size. • If the size distribution of particles is known, the overall collection efficiency of a cyclone can be predicted by using above graph. •Theodore and DePaola (1980) have fitted an algebraic equation to above graph, which makes Lapple’s approach more precise and more convenient for application to computers. Prof S S Jahagirdar, NKOCET 19
  • 20. Prof S S Jahagirdar, NKOCET 20
  • 21. Equation for efficiency X 100 in % Prof S S Jahagirdar, NKOCET 21
  • 22. Prof S S Jahagirdar, NKOCET 22
  • 23. Advantages i) ii) iii) iv) v) low initial cost, simple in construction and operation, low pressure drop, low maintenance requirements, continuous disposal of solid particulate matter, and vi) use of any material in their construction that can withstand the temperature and pressure requirements. Prof S S Jahagirdar, NKOCET 23
  • 24. Disadvantages i) low collection efficiency for particles below 5 – 10 µ in diameter, ii) severe abrasion problems can occur during the striking of particles on the walls of the cyclone, and iii) a decrease in efficiency at low particulate concentration. Prof S S Jahagirdar, NKOCET 24
  • 25. Operational problems • i) Erosion: Heavy, hard, sharp edged particles, in a high concentration, moving at a high velocity in the cyclone, continuously scrap against the wall and can erode the metallic surface. Prof S S Jahagirdar, NKOCET 25
  • 26. • ii) Corrosion: If the cyclone is operating below the condensation point, and if reactive gases are present in the gas stream, then corrosion problems can occur. Thus the product should be kept above the dew point or a stainless steel alloy should be used. • iii) Build – up: A dust cake builds up on the cyclone walls, especially around the vortex finder, at the ends of any internal vanes, and especially if the dust is hygroscopic. It can be a severe problem. Prof S S Jahagirdar, NKOCET 26
  • 27. Applications of cyclones i) For the control of gas borne particulate matter in industrial operations such as cement manufacture, food and beverage, mineral processing and textile industries. ii) To separate dust in the disintegration operations, such as rock crushing, ore handling and sand conditioning in industries. iii) To recover catalyst dusts in the petroleum industry. iv) To reduce the fly ash emissions. Prof S S Jahagirdar, NKOCET 27
  • 28. • Applications • • • • • • • • • • Power Plant Textile industry (Cotton, Polyester) Stone Crusher Mineral Industry Rubber Industry Material Handling Fly Ash Lead Industry Cement Industry Steel Industry Prof S S Jahagirdar, NKOCET 28
  • 29. Objective Questions Q1. In cyclone particulate separation takes place because of ________________ force. Q2. Cyclone separator has ___________ inlet. Q3. In case of cyclone equation for effective turns is given by _______________. Q4. Cut size diameter in case of cyclone can be computed by using equation _______________. Q5. In case of a standard cyclone length of conical part is given by ________________. (similar questions on dimensions of cyclone) Prof S S Jahagirdar, NKOCET 29
  • 30. Theory Questions Q1. Discuss with neat sketch working principle of cyclone. Also list its advantages and disadvantages. Q2. write short notes on:1. Standard cyclone 2. Operational problems in cyclone. 30 Prof S S Jahagirdar, NKOCET
  • 31. Prof S S Jahagirdar, NKOCET 31
  • 32. Prof S S Jahagirdar, NKOCET 32