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Equipment to Control
Particulate Metter [part-2]
Ravi Kumar GARRE
Contents covered
• Introduction
• Settling chambers
• Inertial separators
• Cyclones
• Filters
• Electrostatic precipitators
• Scrubbers/ wet collectors
[Note: settling chambers, inertial separators,
cyclones are not covered in this presentation]
Introduction
• To remove particulate matter from gaseous
streams various types of equipments are in
practice.
 Settling chambers
 Inertial separators
 Cyclones
 Filters
 Electrostatic precipitators
 Scrubbers/ wet collectors
Introduction
• The data to keep in mind in the
selection of proper equipment is:
 Quantity of gas to be treated and its variation
with time
 Nature of particulate matter
 Concentration of particulate matter
 Temperature and pressure of gas stream
 Nature of gas stream (i.e. solubility, corrosivity,
ignitability, etc.)
 Desired quality of treated effluent
Introduction
• Objectives of control equipment
 Prevention of nuisance
 Prevention of physical damage to property
 Recovery of valuable waste product
 Minimization of economic losses
• Efficiency of separating device
η = (quantity of particulates collected
from gas)/(quantity of particulates
present initially)
Filters
• Filters (or) fabric filters,
also called as fabric
collectors/ cloth filters/
bag filters/ bag house.
• Fabric collectors use
filtration to separate
particulates from
polluted gas streams.
Filters
• Polluted gases enter the bag
house and pass through
fabric bags that act as filters.
• The bags can be of woven,
cotton, synthetic or glass-
fibre material in either a
tube or envelope shape.
• In this system, the entered
gas allowed to pass through
these bags, which filters out
the particulate matter and
allows the gas to escape.
Fabric filters
• Small particles are
retained on the fabric,
later on when the dust
mat will be formed.
• Frequently the bags/ filter
material should be
cleaned or replaced.
• Small particles can retain
in the bags.
• Fabric filters can remove
particle of size about
1µm.
Fabric filters
• Fabric filters are 99 % efficient in removing
particles of size 1µm to 10µm
• The factors affecting efficiency is:
 Improper selection of filter media
 Temperature of gaseous stream
 Particle size of particulate matter
Fabric filters
Advantages
• Higher collection efficiency
• It collects particles smaller than 10µm
• Requires normal power consumption
Disadvantages
• High temperature gases need to be cooled
• High initial and maintenance cost
• High fabric replacement cost
• Large size equipment
• Fabric is liable to chemical attack
Fabric filters
Applications
• Metallurgical industry
• Foundries
• Cement industry
• Ceramic industry
• Flour mills
• Brick works
Electrostatic precipitators
• Electrostatic precipitator is a device that
removes suspended dust particles from a gas
or exhaust by applying a high-voltage
electrostatic charge and collecting the
particles on charged plates
• Electrostatic precipitators can remove
particles of size less than 1µm
• Efficiency – 95 to 99%
Electrostatic precipitators
• In this method two electrodes are
fitted inside a chamber.
• When high voltage is applied an
electric discharge takes place in
between these two plates as a
result a strong electromagnetic
field will be created.
• The air in the strong
electromagnetic field get ionised.
• The ionised air consists of ions
and free electrons.
Electrostatic precipitators
Electrostatic precipitators
• If the polluted gas allowed to pass through the
strong electromagnetic filed, the particulate
matter get negatively charged and attracted to
positively charged electrodes.
• Therefore, the particulate matter settle down
on the surfaces of electrode plates.
• These can be dislodged by vibrating the
electrodes.
Electrostatic precipitators
Electrostatic precipitators
Components of ESP
• A Source of high voltage
• Electrode plates
• Inlet and outlet for the gas
• A hopper for disposal of
collected gases
• A cleaning system
• An outer casing to form an
enclosure around the
electrodes
Electrostatic precipitator
Advantages
• Particles may be collected wet or dry
• Even small particles can be removed
• They can be operated at high temperatures up to 450 ˚C
• Maintenance is nominal
Disadvantages
• Higher initial costs
• Sensitive to variable dust loadings and flow rates
• Collection efficiency reduces with time
Electrostatic precipitator
Applications
• Cement factories
• Pulp and paper industries
• Steel plants
• Non-ferrous metal industry
• Chemical industry
• Petroleum industry
• Power plants
Scrubbers
• Scrubbers are also called as wet collectors.
• Scrubbers utilise liquids (generally water) to
assist in the removal of particulates from the
carrier gas stream.
• In wet collectors, the particulate matter is
agglomerated with water and then separated
from the gas with water.
• Scrubbers can separate particles even smaller
than 0.2µm.
Spray towers
• Spray tower is the simplest
type of wet scrubber.
• In this scrubber, gas is
passed counter current to
falling drops of liquid from
a series of nozzles.
• The impingement and
interception of particles
with liquid droplets cause
settlement of particles
along with liquid droplets.
• Spray towers are used to
separate coarser particles.
Cyclone scrubbers
• Cyclone scrubbers are
another types of wet
collectors.
• High pressure nozzle
sprays located inside the
chamber generate a fine
spray that intercepts
particles entrained in the
swirling gases.
• The particulate matter is
thrown on to the walls by
centrifugal action and then
drained to the bottom.
Scrubbers/ wet collectors
Advantages
• Simultaneously remove particulates as well as
gaseous pollutants
• Hot gases can be cooled down
• Corrosive gases can be recovered and neutralised
Disadvantages
• Lot of waste water produced
• Maintenance cost is high
Choice of equipment
1. Particulate size
2. Particulate loading
3. Required efficiency
4. Properties carrier gas: Composition,
Temperature, Pressure, Viscosity, Density,
Humidity, ignitability, reactivity, electrical
property, etc.
5. flow characteristics of carrier gas
6. Capital and operating cost of equipment
7. Ease of maintenance and reliability
Economic aspects
THANK YOU

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Equipment to control particulates part 2

  • 1. Equipment to Control Particulate Metter [part-2] Ravi Kumar GARRE
  • 2. Contents covered • Introduction • Settling chambers • Inertial separators • Cyclones • Filters • Electrostatic precipitators • Scrubbers/ wet collectors [Note: settling chambers, inertial separators, cyclones are not covered in this presentation]
  • 3. Introduction • To remove particulate matter from gaseous streams various types of equipments are in practice.  Settling chambers  Inertial separators  Cyclones  Filters  Electrostatic precipitators  Scrubbers/ wet collectors
  • 4. Introduction • The data to keep in mind in the selection of proper equipment is:  Quantity of gas to be treated and its variation with time  Nature of particulate matter  Concentration of particulate matter  Temperature and pressure of gas stream  Nature of gas stream (i.e. solubility, corrosivity, ignitability, etc.)  Desired quality of treated effluent
  • 5. Introduction • Objectives of control equipment  Prevention of nuisance  Prevention of physical damage to property  Recovery of valuable waste product  Minimization of economic losses • Efficiency of separating device η = (quantity of particulates collected from gas)/(quantity of particulates present initially)
  • 6. Filters • Filters (or) fabric filters, also called as fabric collectors/ cloth filters/ bag filters/ bag house. • Fabric collectors use filtration to separate particulates from polluted gas streams.
  • 7. Filters • Polluted gases enter the bag house and pass through fabric bags that act as filters. • The bags can be of woven, cotton, synthetic or glass- fibre material in either a tube or envelope shape. • In this system, the entered gas allowed to pass through these bags, which filters out the particulate matter and allows the gas to escape.
  • 8. Fabric filters • Small particles are retained on the fabric, later on when the dust mat will be formed. • Frequently the bags/ filter material should be cleaned or replaced. • Small particles can retain in the bags. • Fabric filters can remove particle of size about 1µm.
  • 9. Fabric filters • Fabric filters are 99 % efficient in removing particles of size 1µm to 10µm • The factors affecting efficiency is:  Improper selection of filter media  Temperature of gaseous stream  Particle size of particulate matter
  • 10. Fabric filters Advantages • Higher collection efficiency • It collects particles smaller than 10µm • Requires normal power consumption Disadvantages • High temperature gases need to be cooled • High initial and maintenance cost • High fabric replacement cost • Large size equipment • Fabric is liable to chemical attack
  • 11. Fabric filters Applications • Metallurgical industry • Foundries • Cement industry • Ceramic industry • Flour mills • Brick works
  • 12. Electrostatic precipitators • Electrostatic precipitator is a device that removes suspended dust particles from a gas or exhaust by applying a high-voltage electrostatic charge and collecting the particles on charged plates • Electrostatic precipitators can remove particles of size less than 1µm • Efficiency – 95 to 99%
  • 13. Electrostatic precipitators • In this method two electrodes are fitted inside a chamber. • When high voltage is applied an electric discharge takes place in between these two plates as a result a strong electromagnetic field will be created. • The air in the strong electromagnetic field get ionised. • The ionised air consists of ions and free electrons.
  • 15. Electrostatic precipitators • If the polluted gas allowed to pass through the strong electromagnetic filed, the particulate matter get negatively charged and attracted to positively charged electrodes. • Therefore, the particulate matter settle down on the surfaces of electrode plates. • These can be dislodged by vibrating the electrodes.
  • 17. Electrostatic precipitators Components of ESP • A Source of high voltage • Electrode plates • Inlet and outlet for the gas • A hopper for disposal of collected gases • A cleaning system • An outer casing to form an enclosure around the electrodes
  • 18. Electrostatic precipitator Advantages • Particles may be collected wet or dry • Even small particles can be removed • They can be operated at high temperatures up to 450 ˚C • Maintenance is nominal Disadvantages • Higher initial costs • Sensitive to variable dust loadings and flow rates • Collection efficiency reduces with time
  • 19. Electrostatic precipitator Applications • Cement factories • Pulp and paper industries • Steel plants • Non-ferrous metal industry • Chemical industry • Petroleum industry • Power plants
  • 20. Scrubbers • Scrubbers are also called as wet collectors. • Scrubbers utilise liquids (generally water) to assist in the removal of particulates from the carrier gas stream. • In wet collectors, the particulate matter is agglomerated with water and then separated from the gas with water. • Scrubbers can separate particles even smaller than 0.2µm.
  • 21. Spray towers • Spray tower is the simplest type of wet scrubber. • In this scrubber, gas is passed counter current to falling drops of liquid from a series of nozzles. • The impingement and interception of particles with liquid droplets cause settlement of particles along with liquid droplets. • Spray towers are used to separate coarser particles.
  • 22. Cyclone scrubbers • Cyclone scrubbers are another types of wet collectors. • High pressure nozzle sprays located inside the chamber generate a fine spray that intercepts particles entrained in the swirling gases. • The particulate matter is thrown on to the walls by centrifugal action and then drained to the bottom.
  • 23. Scrubbers/ wet collectors Advantages • Simultaneously remove particulates as well as gaseous pollutants • Hot gases can be cooled down • Corrosive gases can be recovered and neutralised Disadvantages • Lot of waste water produced • Maintenance cost is high
  • 24. Choice of equipment 1. Particulate size 2. Particulate loading 3. Required efficiency 4. Properties carrier gas: Composition, Temperature, Pressure, Viscosity, Density, Humidity, ignitability, reactivity, electrical property, etc. 5. flow characteristics of carrier gas 6. Capital and operating cost of equipment 7. Ease of maintenance and reliability