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A O[r O @ MO@[n)
►A simplest device, collecting dust
of size
>1oµm.
►Settling chambers use the force of
gravity to remove solid particles. The gas
stream
enters a chamber where the velocity of
the gas is reduced. Large particles drop D
f
e
r
t
J
;
:
s
o
u
t of the gas and are recollected in
hoppers. Because settling chambers are
effective in removing only larger
particles, they are used in conjunction
with a more efficient control device.
►T
h
e size, shape of particles and density
and viscosity are important parameters.
C
l
e
a
nG
a
s
Exits
. ---···
PROCESS CYCLONE SCHEMATIC...---1
This process is achieved by a sudden
change in the direction of gas flow.
The dust particle is spinning in a
circular path, it is subjected to an
outward force. As a result the
particles collect on the wall and fall
to the bottom of the vessel.
DIRTY
GAS
'
DUST
-
---
►Passing the particle laden gases Figure9.
between high voltage discharge Tranf_ormer-
e
1ectrod es.
Rect1f1er"'-'
Sets
►Majority of particles
get charged
and collected on ground
electrodes.
►Atintervals both discharge and c1 :
collecting electrodes are rapped to Out
dislodge collected particles from
the electrodes, which then fall into
hoppers at the bottom of the
precipitator.
►Ele. Precipitator is efficient for
the particle size below o.01µm,
can tolorate operating
temperature as high as 700°k.
ConventionalElectrostatic Precipitator
.., _,..Rappers
.,...._Collection
Plates
Hoppers _J,.,.,;;,.....--·
Flue Gas In
Discharge
Electrodes
=
=
:
This method is most often used type of
device, which is required to meet
any future standards limiting the
emission of respirable particles.
The collection efficiency is very high
and even for particle of o.01µm
diameter.
The Fabric filters, or bag houses ,
remove dust from a gas stream by
passing the stream through a porous
fabric.
The fabric filter is efficient at removing
exceed
most
fine particles and can
efficiencies of 99% in
applications.
Figure13. Reverse AirFabricFilter
Induced
6
Draft
rt---'!Fan
Gas
Ol.lllet
.. . B
a
g
GasInlet
Compartment3
Compartment 2
Compartment 1
=·=:.. '-
Objective of scrubber is to
entrain the particulate matter
bottom of the scrubber,
in liquid droplets. Water
subsequently flows from the
the
particulate is allowed to settle
and clarified water is re
circulated.
SCRUBBING CUTAWAY
DIRTY
GAS
INLET
CLEAN GAS O UTL E T
i , + - - S C R U B B I N G
MEDIUM
SPRAYS
, . ) = : : - S C R U B B E R
BODY
SCRUBBING LIQUOR A ND
RE CO V E R ED D U S T O UTL E T
Area
category
Suspended
particulate
matter
S02 co N02
Industrial
and mixed
use
500 120 5000 120
Residential
and Rural
200 80 2000 50
Sensitive
area (tourist
resort, game
sanctuary)
100 30 1000 30
(concentration in pgm3)
Vehicle at manufacturing stage 60 Hatridge Smoke Units (HSU)
Vehicle on road 70 HSU
Category Vehicle on
road
Vehicle at
manufacturing
stage
2 or 3 wheeler
vehicles with
engine
displacement less
than 50cc
5.0 5.0
Other 2 or 3
wheelers
4.5 5.5
4 wheelers 4.0 3.5
: : . - - - - ---
Diesel driven vehicles: (Smoke density)
---
Petrol driven vehicles: (Limits of CO in percentage
volume)
selecte
I I
Liquid In
' , j
Absorber or
stripping C-olumn
'
•
Gas Out
Liquid Out - G n l n
fOsorption is a process where gases,
vapours or liquids are concentrated
on a solid surface as a result of
surface or chemical force (physical
adsorption
respectively).
and chemisorptions
The amount of
adsorbed substances depends
directly on the internal surface area
of solid and the l<inetics of the
process.
The most important adsorbents in
industrial use to-days are Bauxite,
activated carbon, activated alumina,
silica gel and molecular sieves.
OityGas
CIJGI,
.--1 SIMmfor
Regenetllloc,
I
CondtnNII CM
♦
voe
(tciuene.etc..) I
I
I
I
(Alst.artup) l£.u!!jg )
,.-- -·
I
II
I
•
I
•
' ' '
i'i
>
u
.rtti.
.
cd11r.
m
m
m
Concentration equipment
air-pollution-control-74445648.pptx
air-pollution-control-74445648.pptx
air-pollution-control-74445648.pptx

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air-pollution-control-74445648.pptx

  • 1.
  • 2.
  • 3.
  • 4.
  • 5.
  • 6. A O[r O @ MO@[n)
  • 7.
  • 8.
  • 9.
  • 10.
  • 11.
  • 12.
  • 13. ►A simplest device, collecting dust of size >1oµm. ►Settling chambers use the force of gravity to remove solid particles. The gas stream enters a chamber where the velocity of the gas is reduced. Large particles drop D f e r t J ; : s o u t of the gas and are recollected in hoppers. Because settling chambers are effective in removing only larger particles, they are used in conjunction with a more efficient control device. ►T h e size, shape of particles and density and viscosity are important parameters. C l e a nG a s Exits
  • 14. . ---··· PROCESS CYCLONE SCHEMATIC...---1 This process is achieved by a sudden change in the direction of gas flow. The dust particle is spinning in a circular path, it is subjected to an outward force. As a result the particles collect on the wall and fall to the bottom of the vessel. DIRTY GAS ' DUST
  • 15. - --- ►Passing the particle laden gases Figure9. between high voltage discharge Tranf_ormer- e 1ectrod es. Rect1f1er"'-' Sets ►Majority of particles get charged and collected on ground electrodes. ►Atintervals both discharge and c1 : collecting electrodes are rapped to Out dislodge collected particles from the electrodes, which then fall into hoppers at the bottom of the precipitator. ►Ele. Precipitator is efficient for the particle size below o.01µm, can tolorate operating temperature as high as 700°k. ConventionalElectrostatic Precipitator .., _,..Rappers .,...._Collection Plates Hoppers _J,.,.,;;,.....--· Flue Gas In Discharge Electrodes
  • 16. = = : This method is most often used type of device, which is required to meet any future standards limiting the emission of respirable particles. The collection efficiency is very high and even for particle of o.01µm diameter. The Fabric filters, or bag houses , remove dust from a gas stream by passing the stream through a porous fabric. The fabric filter is efficient at removing exceed most fine particles and can efficiencies of 99% in applications. Figure13. Reverse AirFabricFilter Induced 6 Draft rt---'!Fan Gas Ol.lllet .. . B a g GasInlet Compartment3 Compartment 2 Compartment 1
  • 17. =·=:.. '- Objective of scrubber is to entrain the particulate matter bottom of the scrubber, in liquid droplets. Water subsequently flows from the the particulate is allowed to settle and clarified water is re circulated. SCRUBBING CUTAWAY DIRTY GAS INLET CLEAN GAS O UTL E T i , + - - S C R U B B I N G MEDIUM SPRAYS , . ) = : : - S C R U B B E R BODY SCRUBBING LIQUOR A ND RE CO V E R ED D U S T O UTL E T
  • 18.
  • 19. Area category Suspended particulate matter S02 co N02 Industrial and mixed use 500 120 5000 120 Residential and Rural 200 80 2000 50 Sensitive area (tourist resort, game sanctuary) 100 30 1000 30 (concentration in pgm3)
  • 20. Vehicle at manufacturing stage 60 Hatridge Smoke Units (HSU) Vehicle on road 70 HSU Category Vehicle on road Vehicle at manufacturing stage 2 or 3 wheeler vehicles with engine displacement less than 50cc 5.0 5.0 Other 2 or 3 wheelers 4.5 5.5 4 wheelers 4.0 3.5 : : . - - - - --- Diesel driven vehicles: (Smoke density) --- Petrol driven vehicles: (Limits of CO in percentage volume)
  • 21. selecte I I Liquid In ' , j Absorber or stripping C-olumn ' • Gas Out Liquid Out - G n l n
  • 22.
  • 23. fOsorption is a process where gases, vapours or liquids are concentrated on a solid surface as a result of surface or chemical force (physical adsorption respectively). and chemisorptions The amount of adsorbed substances depends directly on the internal surface area of solid and the l<inetics of the process. The most important adsorbents in industrial use to-days are Bauxite, activated carbon, activated alumina, silica gel and molecular sieves. OityGas CIJGI, .--1 SIMmfor Regenetllloc, I CondtnNII CM ♦
  • 24.
  • 25. voe (tciuene.etc..) I I I I (Alst.artup) l£.u!!jg ) ,.-- -· I II I • I • ' ' ' i'i > u .rtti. . cd11r. m m m Concentration equipment