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air pollution.pdf
1. AIR POLLUTION CONTROL
1. Objectives
2. Basic approach
3. Control equipments
4. Gaseous pollutant control
5. Particulate pollutant control
5. Particulate pollutant control
2. Air Pollution Control
Objectives:
1. Prevention of nuisance
2. Prevention of physical damage to property
3. Elimination of health hazards
4. Recovery of valuable waste products
4. Recovery of valuable waste products
5. Product quality improvement
6. Minimization of economical losses in the
industrial maintenance
3. Basic Approach
Pollution control could be achieved by adopting
two approaches such as:
1. Dilution of pollutants to permissible level
2. Confining the pollutants at source
Dilution of pollutants to permissible level
Dilution of pollutants to permissible level
I. Use of tall stacks
II. Dispersion of source locations
Confining the pollutants at source
I. Process control
II. Pollutant control
4. Process control:
The process is modified in such a way that the
pollutants do not form at all beyond the
permissible concentration.
It is the most effective way of pollution control.
However it is some what expensive.
It could be done by two ways as under:
It could be done by two ways as under:
i) Raw material changes
ii) Operational changes
Operational changes could be done either by
more effective operation of existing machinery
or by replacement of old machinery.
5. Pollutant control:
When process control fails to achieve the
source correction the pollution can be
controlled by adopting effluent gas
cleaning techniques, which involves many
chemical engineering unit operations.
chemical engineering unit operations.
At present it is the main pollution control
technology and it is of following two types:
1. Gaseous pollution control technology
2. Particulate pollution control technology
6. Gaseous pollution control technology
Gaseous pollution control could be
achieved by adopting any one of the
following three methods depending upon
the nature of pollutant (effluent) gas.
1. Combustion
1. Combustion
2. Absorption
3. Adsorption
7. 1. Combustion
Conditions: This technique is used when the
effluent gas contains organic pollutants. Product
of combustion are CO2 & H2O vapors (less harm)
Process: 1. Thermal (Flame) combustion
2. Catalytic combustion:-carried out when lower
operating temperature is desirable. Ex- coffee
operating temperature is desirable. Ex- coffee
roasting, enamel baking, paint fumes, waste gas
Equipments:
1. Thermal combustors-fume incinerators, steam
injection(ventury)flares, after burners, etc
2.Catalytic combustors-
11. 2. Absorption
Conditions: This technique is widely used
when the effluent gas contains hazardous
pollutants like NOx, SOx, H2S, Fluorides, etc
Process: The effluent gas is passed through a
suitable liquid adsorbent like aq. NaOH, aq.
suitable liquid adsorbent like aq. NaOH, aq.
HNO3, liquor NH3, NaOH+Phenol,
Ethanolamine di Me Aniline, etc. One or
more pollutants get absorbed / modified.
Equipments: Plate towers, packed towers,
spray towers, bubble cap towers, scrubber
towers, etc
16. Absorption… cont …
Efficiency:
Depends upon following factors-
1. Chemical reactivity of the
pollutants in liquid phase
pollutants in liquid phase
2. Extent of surface contact between
gas & liqid
3. Time of contact
4. Concentration of absorbing
medium
17. 3. Adsorption
Conditions: This technique is used when the
effluent gas contains pollutants like NOx, SOx,
HF,Org.solvent vapors, Petroleum fractions, etc
Process: The effluent gas is passed through a
porous solid adsorbent like Silicagel, Zeolite,
Dolomite, Bauxite, Alumina, Limestone lumps,
Dolomite, Bauxite, Alumina, Limestone lumps,
NaF pallets, Iron oxide, Activated Carbon, etc.
Both the Organic & Inorganic pollutants are
held over the interface of the solid adsorbent by
physical adsorption or chemo sorption.
18. Adsorption… cont …
Equipment:-
Consists of a packed adsorbent in the middle
region.
It has one inlet for effluent gas below the bed.
Regenerative System:-
Regenerative System:-
The equipment is also provided with a
regenerative system, which causes disorption of
the Adsorbate pollutants on raising temperature
by injecting super heated steam or reducing
pressure.
20. Adsorption… cont …
Efficiency:- Depends upon the following factors
1. Surface area per unit weight of adsorbent.
2. Chemical nature of adsorbent.
3. Nature & concentration of adsorbate pollutant
4. Extent and time of contact of adsorbent &
adsorbate
adsorbate
Advantages:-
1. Though installation cost of equipment is high,
the operation & maintenance cost is quit low.
2. Some time the value of recovered adsorbate
material enhances economic feasibility.
21. Activated Carbon Adsorber
Adsorption Capacity: Activated Carbon acts as a
very good adsorbent because it is a highly
porous solid & provides a very large surface
area for adsorption (surface area of 1cubic inch
activated carbon is above 20,000 sq. meters).
This surface area is far greater than the volume
This surface area is far greater than the volume
of the adsorbate to be adsorbed.
Adsorption Selectivity: i) The adsorption by
activated C is primarily a physical phenomenon
ii) Most suitable for Org. solvent vapours (HCs)
iii) Only adsorbent that adsorbs toxic & odorous
materials (other methods are impossible/hazardous/uneconomical)
22. Particulate pollution control technology
Particulate matter emitted in effluent gases are
minute suspended particles of 0.1 to 100 µm
diameter.
These are originated from stationary as well as
mobile sources.
mobile sources.
Depending on their characteristics such as:-
i) size & shape ii) physical & chemical nature
iii) concentration iv) hygroscopic property v)
electrical properties and vi) toxicity
the choice of devices to be used is based.
23. Particulate pollution control tech …cont…
Pollution Control Equipments:
1. Mechanical devices-cyclone collector, gravity
separator, etc
2. Absorption devices- wet scrubbers
3. Filtration devices- fabric filers
3. Filtration devices- fabric filers
4. Electrical devices- electrostatic precipitators
Generally the spm of bigger dimension(< 50µm)
are removed by Cyclone separators & Wet scrubbers
where as fine spm (>0.1µm) are removed by
fabric filers & ectrostatic precipitators
24. 1. Cyclone Separators
Principle: Utilizes a centrifugal force generated
by spinning gas stream which separates the spm
from the career gas.
Equipment: Consists of a vertical cylinder with a
conical bottom.
Near the top a tangential inlet for effluent gas is
Near the top a tangential inlet for effluent gas is
located and at the bottom of the cone an outlet
for spm is provided.
An outlet pipe for clean gas is extended in to
cylinder to prevent short circuiting of gas from
inlet to outlet.
26. Cyclone Separators … cont …
Operation:
The effluent gas upon entering the cyclone
cylinder, receives a rotating motion.
The vortex so formed, develops a centrifugal
force, which acts through the spm radically
force, which acts through the spm radically
towards the cylinder wall.
The gas spirals down wards to the bottom of the
cone and at the bottom, the gas flow reverses to
form an inner vortex, which leaves through the
outlet pipe.
27. Cyclone Separators … cont …
Applications:
Used to remove the bigger spm from
1. Rock product industries- cement, mining,
mineral processing, power plant fly ash, etc
2. Iron & Steel plants
3. Metallurgical industries
4. Food processing
5. Textile & paper industries
6. Petroleum refineries- recovery of catalyst
28. Cyclone Separators … cont …
Advantages:
1. Low initial cost
2. Simple installation
3. Easy operations
4. Low maintenance cost
4. Low maintenance cost
5. Continuous dust disposal
Limitations:
1. Not applicable for separation of fine spm
2. Low collection efficiency (50 to 90%) for the
separation of bigger spm too.
29. 2. Wet Scrubbers
Principle:The spm laden gas is passed through a
fine spray of water that very effectively removes
spm as well as some gaseous matter.
Equipment: Gravity spray scrubbers, Cyclone
spray scrubbers, Wet centrifugal scrubbers, wet
imprigner scrubbers, Ventury scrubbers, etc
imprigner scrubbers, Ventury scrubbers, etc
System: spm collection could be done by-
1. Liquid carriage type method:- The spm laden
gas stream is allowed to strike a liquid surface
within the collector and the liquid carrying the
trapped gas / spm move to a location outside the
collector for ultimate disposal.
31. Wet Scrubbers … cont …
2.Particle conditioning type :- spm in gas stream
are brought in to intimate contact with water so
that effective size of spm is increased due to
formation of heavier water spm agglomerates
that can be more easily separated from the gas
stream by any of the collection mechanism.
stream by any of the collection mechanism.
Conditions: Wet scrubbers are used when-
1. Gaseous pollutants are to be removed along
with the spm
2. Effluent gas to be treated is combustible
3. Temperature of effluent gas is above 300 Oc
32. Wet Scrubbers … cont …
4. Cooling is desired and water addition is not
objectionable.
5. Volume of the treated gas is low.
6. Large variations in process flow rates have to
be accommodated.
be accommodated.
Applications:
1. Chemical industries- H2SO4 manufacture
2. Mining & metallurgical industries
3. Craft mill furnaces
4. Petroleum refineries
33. Wet Scrubbers … cont …
Advantages:
1. Low initial cost
2. High collection efficiency
3. Applicable for hot effluent gases (> 300 Oc)
4. Along with spm gaseous pollutants such as
4. Along with spm gaseous pollutants such as
NH3, SOx, Metal fluons, etc are also removed
Limitations:
1. High power consumption
2. High maintenance cost(due to corrosion & abrasion)
3. Water & soil pollution (due to wet disposal)
34. 3. Fabric Filters
Principle: spm laden gases are forced through a
porous medium such as woven / felted fabrics.
The spm are trapped due to different physical
mechanism such as inertial impaction, direct
interception, diffusion, etc. The clean gas is
discharged out.
discharged out.
Filtration System: Filtration is the oldest, one of
the most versatile & efficient methods for
removing spm from the industrial gases.
Fabric filters may be woven fabrics or felt cloth.
Wovenfabrics have definite long range repeating
35. Fabric Filters …cont…
Pattern and considerable porosity in the
direction of gas flow. Felted cloth consists of
randomly oriented fibers compressed in to a mat
on a loosely woven backing material.
Conditions: The choice of fabric filter is based
primarily on the:- I. Operating temperature
primarily on the:- I. Operating temperature
II. Corrosiveness/abrasiveness of the spm
At low temp (80-90Oc)- Cotton & Nylon
At high temp (250-350Oc)- Asbestos & Si coated
For acidic gases-Wool, Orlon, Vinyon, etc
For alkaline media- Asbestos & Nylon
For High chemical resistance- glass fibers
37. Fabric filter: Equipment
Equipment: A typical fabric filter consists of a bag
house made of tubular bags mounted on shaking
manifold in such a manner that the suspended particles
fall in to a hoper when dislodged from the fabrics.
The effluent gas inlet is situated at lower portion while
the outlet for clean gas is at upper portion and the dust
the outlet for clean gas is at upper portion and the dust
outlet is at the bottom of the hoper.
Operation: Particle laden gas enters the bags at bottom
and passes through the fabrics. The spms deposit on
the insides of the bags while the clean gas passes out.
Cleaning of the bags is carried out by shaking and the
spms from hoper are taken out at fixed intervals.
38. Fabric filter: Equipment
Applications:
1. Pigment and paint industries.
2. Pharmaceutical plants.
3. Metallurgical industries
4. Rock product industries- clay,
ceramics, cement, carbon black, etc.
Limitations:
1. High fabrication cost due to the large
size of the equipment (bag house).
2. High fabrication cost due to fabric
replacement
39. Fabric filter: Equipment
Advantages:
1. Very high collection efficiency
(99 to 99.99%)
2. Collection of spm in dry state
3. Useful for fine spm in particular
3. Useful for fine spm in particular
4. Simple installation
5. Simple operation
6. Low pressure drop
7. Low power consumption
40. Electrostatic precipitators
Principle:
The spm in gas stream are charged electrically over
the high voltage electrodes and under the influence of
electric field, separated from the gas stream.
Electric device:
Electrostatic precipitators consist of following parts:
Electrostatic precipitators consist of following parts:
• A source of high voltage for charging the particles
electrically by ionization
• High voltage discharge electrode (usually -ve) of
small cross sectional area (wire) and a collecting
electrode (usually +ve) of large surface area
(tube/plate) and lower potential.
41. Electrostatic precipitators
• A device for disposing the collected particles.
• An outer housing enclosing the electrodes.
Operation:
It involves four basic steps as under:
1. Charging- The particulates in incoming gas
1. Charging- The particulates in incoming gas
are charged electrically over the high
voltage electrodes by ionization.
2. Transporting- The charged particulates are
transported by the force exerted upon them
in the electric field to the collecting surface.
42. Electrostatic precipitators
3. Discharging- The charged spm are precipitated on
the collecting surface by the neutralization of their
electric charge.
4. Removal- The precipitated spm from the collecting
surface are removed by wrapping or washing.
Applications:
Applications:
1. Two stage precipitators- First stage is ionization
and the second one is precipitation. This type device is
most widely used in air conditioning plants.
2. One stage precipitators- Ionization & precipitation
are performed in a single step. This type of devices are
suitable for heavy dust concentration and hence used
45. Electrostatic precipitators
These are used in following industries
1. Power plants
2. Pulp & paper industries
3. Iron & steel plants
4. Chemical industries- Sulphuric acid
4. Chemical industries- Sulphuric acid
manufacturing plants
5. Refineries
6. Mining & metallurgical industries
7. Rock product industries- Cement,
ceramics, carbon black, etc.
46. Electrostatic precipitators
Advantages:
1. High collection efficiency (80 – 99.5%)
2. Applicable for efficient removal of the fine spm
3. Applicable for very large volumes of industrial
effluent gases.
4. Applicable for high temperature industrial gases
5. Valuable dry particulate matter could be removed
6. Low maintenance cost
7. Low power consumption
8. Negligible treatment time
9. Low pressure drop.