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Environmental Aspects of Power
Generation
Various kinds of fuel may be burned inthermal power plants, all of which releaseemissions into the air.
Some fuels that are well known includefossil fuels:
Coal Natural gas, Oil
Methane (produced by biomass) andwood waste.
Non-fossil : Nuclear
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The emissions can vary dramatically,
depending upon the fuel being burned and
the plant technology.
Some of the environmental impacts which may be
associated with thermal power plants include:
Air pollution/airborne emissions, including
particulates, toxics, greenhouse gases and
heat Risk of spills of fuel on land, or
contamination of water or groundwater
Noise pollution
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The Thermal Plants produce emissions :
1. Fossil Power Plants
Sulfur Oxides(SOx) Nitrogen Oxides(NOx)
Carbon Oxides(CO2,CO)
Particulate Matter Thermal Pollution
2. Nuclear Power Plants Radioactivity release
Radioactive waste
Thermal pollution
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Air Pollution
Definition:
Any atmospheric condition in which certainsubstances are present in such concentrationsthat they can produce undesirable effects on
man and his environment.
The substances include- Gases ( SOx , NOx, CO, CO2, HCs)
- Particulate matter(smoke, dust, fumes, aerosols)
- Radioactive materials etc.
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TYPES OF AIR POLLUTANTS
Primary pollutants are emitted directly from the
sources into the atmosphere, which include:
Particulate matter: Ash, Smoke, Dust, Fumes, Mist andSpray
Inorganic gases: SOx, H2S, NOx, NH3, CO,CO2, & H2F
Olefinic and aromatic hydrocarbons; and
Radioactive compounds
The primary pollutants in sufficient concentrations
to be of immediate concern are:
Particulate matter, SOx, NOx, CO, and HCs.
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Secondary Pollutants
Generated over time in the atmosphere from
chemical reactions involving primary pollutants.
The secondary pollutants include:
SO3, NO2, Peroxyacetylnitrate(PAN),
O3, Aldehydes, Ketones, and various
sulphate & nitrate salts.
Secondary pollutants are formed from chemical
and photochemical reactions in the atmosphere.
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The reaction mechanisms are influenced by such
factor as
Concentration of reactants
Degree of photo-activation
Local topography
Meteorological forces and
Moisture content in atmosphere
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Sources of air pollutants
Industry
Fossil fuel combustion, smelting
Transport
Fossil fuel combustion
Agriculture
Animal effluent, fertilizers,
biomass burning
Domestic
Fossil fuel combustion
Pointand
Diffuse
sources
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MAJOR AIR POLLUTANTS
SO2 Gas Fossil fuel combustion, natural
NOx Gases Fossil fuel combustion, natural
CO Gas Fossil fuel combustion
VOCs Gases Cars, organic solvents, natural
NH3 Gas Agriculture, natural
TSP Particulate Oxidation, fossil fuel burning, dust
Heavy
metals
Particulate Metal processing, fossil fuel burning
Acidicaerosols
Particulate Secondary - reactions of pollutants from fossilfuel burning
Ozone Gas Secondaryfrom reaction of NOx and
VOCs(volatile organic carbon) under sunlight
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Air pollutant pathways
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AIR POLLUTION SOURCES, PATHWAYS
AND RECEPTORS
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Sulphur dioxide (SO2)
is a gas produced from burning coal, mainly in
thermal power plants.
Some industrial processes, such as production of
paper, power plants and smelting of metals,produce sulphur dioxide.
It is a major contributor to smog and acid rain.
Sulfur dioxide can lead to lung diseases.
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SO2 is a colourless gas with a characteristic, sharp,pungent odour.
It is moderately soluble in water(11.3g/100ml)forming weakly acidic H2SO3.
It is oxidized slowly in clean air to sulphurtrioxide.
In a polluted atmosphere, SO2 reacts photo-
chemically or catalytically with other pollutantsor normal atmospheric constituents to form SO3,H2S, H2SO4, and salts of H2SO4.
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Nitrogen oxides (Nox NO and NO2)causes smog and acid rain.
It is produced from burning fuels including petrol,
diesel, and coal.
Nitrogen oxides can make children susceptible to
respiratory diseases in winters.
Nitrous oxide(N2O), Nitric oxide(NO) and
Nitrogen dioxide(NO2) are formed in appreciable
quantities in the atmosphere.
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NO is a colorless, odorless gas produced largelyby fuel combustion.
It is oxidized to NO2 in a pollutant atmospherethrough photochemical secondary reaction.
NO2 is a brown pungent gas with an irritatingodor.
NO2 is emitted by fuel combustion and nitric acid
plants
Small concentrations of NO2 are detected in thelower stratosphere( oxidation of NO by Ozone).
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Oxides of Carbon: CO and CO2(largest)
Carbon monoxide (CO): colorless, odorless gas
is produced by the incomplete burning ofcarbon-based fuels including petrol, diesel,wood, natural and synthetic products.
It has affinity towards the hemoglobin of thebloodstream and is a dangerous asphyxiant.
It can slow our reflexes and make us confused andsleepy.
The rate of oxidation of CO to CO2 in the
atmosphere seems to be very slow.
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Carbon dioxide (CO2):is more abundant and is
largely contributed by power plant.
CO2
is the principle greenhouse gas emitted as aresult of human activities such as the burning ofcoal, oil, and natural gases.
Hydrocarbons(HCs)
The gaseous and volatile liquid hydrocarbons are
of particular interest as air pollutants.HCs can be saturated or unsaturated, branched or
straight-chain or ring structure.
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In saturated class, CH4 is by far the most abundant
hydrocarbon constituting about 40-80% of total
HCs present in an urban atmosphere.
The unsaturated class includes Alkenes(Olefins)
and Acetylenes.
Among the alkenes the prominent pollutants are
Ethylene and propane.
The HCs in air by themselves alone cause no
harmful effects.
They are of concern because they undergo
chemical reactions in the presence of sunlight.
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Suspended Particulate Matter (SPM)consists of solids in the air in the form of smoke, dust, and
vapour that can remain suspended for extended periods.
SPM can be suspended droplets or solid particles
or mixtures or the two.
Particulates can be composed of inert or extremely
reactive material ranging in size 0.1-100m.
These reactive materials could be oxidized or may reactchemically with the environment.
SPM is the main source of haze which reduces
visibility.
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The finer of these particles, when breathed in can lodge in
our lungs and cause lung damage and respiratory
problems.
The classification of various particulates include:
DustIt contains particles of 1-200m size.
These are formed by natural disintegration of rock and
soil or by mechanical processes of grinding and spraying.
They have large settling velocities and are removed from
air by gravity and other inertial processes.
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SmokeIt consists of fine particles of 0.01-1m size, which can be liquid or
solid and are formed by combustion or chemical processes.
FumesThese are solid particles of the size ranging from0.1 to1m.
Fumes are normally released from chemical and metallurgical
processes.MistIt made of liquid droplets smaller than 10m which are formed by
condensation in the atmosphere or are released from industrial
operations.
FogIt is the mist in which the liquid is water and is sufficiently dense to
obscure vision.
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AIR POLLUTION CONTROL
Particulate Emission ControlParticle sizes range from 0.1m to 100m.
The choice of collection devices depends upon:
Physical and chemical characteristics of particulates
Particulate size and concentration in the gas
Volume of particulates to be handled and
Temperature and Humidity of gaseous medium
Toxicity and inflammability
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Particulate Control Mechanisms1. Gravitational Settling
2. Centrifugal Impaction3. Inertial Impaction
4. Direct interception
5. Diffusion
6. Electrostatic Precipitation
Particulate Control Equipment1. Gravitational Settling Chambers
2. Cyclone Separators3. Fabric Filters
4. Electrostatic Precipitator
5. Wet Collectors(Scrubbers)
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Gravitational Settling Chambers Used to remove large abrasive particles(> 50) from gas steams
Offer low pressure drop and require low maintenance
Collection efficiency can be improved by inserting several trays
Used as pre-cleaners
The minimum particle size that can be removed from the gas with
100% efficiecy is:
Where QVolumetric flow rate of gas steam
nNo. of trays of L X W X H
p and g densities of particle and gas respectively
min
8
( )p
p g
Qd
nWLg
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CYCLONES
Cyclones operate to collect relatively large sizeparticulate matter from a gaseous streamthrough the use of centrifugal forces.
Dust laden gas is made to rotate in a decreasingdiameter pathway forcing solids to the outeredge of the gas stream for deposition into the
bottom of the cyclone.
Efficiencies of 90% in particle sizes of 10
microns or greater are possible.
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Multiple Cyclones(Multi clone) Smaller particles need lower
air flow rate to separate.
Multiple cyclones allow
lower air flow rate, capture
particles to 2m
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Performance & Collection Efficiency
Linear increases with: particle density, gas
stream velocity, and rotational passes
Linear decrease with fluid viscosity
Exponential increase with particle diameter
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Limitations / Advantages / Problems
Reduces internal access needs
Optimal flow rate difficult to adjust
Prone to internal erosion / corrosion
Operation at elevated temperatures possible
Low efficiency for small diameter material
Hopper recirculation / flow distribution problems
High energy costs for volumetric flow requirements
Dew point agglomeration, bridging, and plugging Few moving parts, few mechanical / electrical ignition
sources
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BAGHOUSES(Fabric Filters)
Baghouses utilize the principles to remove solids
from a gaseous exhaust stream are:Sieving(Direct Interception)
Impaction,
Agglomeration(Diffusion) andElectrostatic Filtration
Baghouses maximize the filtration area byconfiguring the fabric filter media into a seriesof long small-diameter fabric tubes referred toas bags.
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Baghouse are tightly packed into a housing wherein the
dust laden air moves across the bag fabric thereby
removing it from the gas stream and building up a
filter cake which further enhances air cleaning.
The filter cake is removed to hoppers by various shakingmeans.
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Fabric-filter Baghouse
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Performance & Efficiency Parameters
The operating pressure drop across the bags is
described by:
Pressure drop
dP = SeV + KCV2t
where Se = drag coefficient
V = velocity
K = filter cake coefficient
C = inlet dust concentration
t = Collection running time
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Limitations / Advantages / Problems
High collection efficiencies
Internal condensation / corrosion
Over-temperature limitations
Need for internal inspection / access
Possible to have variable flow rates Plugging / short-circuiting / break-through/ collection
media fouling
Accumulation of flammable gases/ dusts and ignitionsources
Unexpected bag failure due to changes in operatingparameters
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ELECTROSTATIC PRECIPITATORS(ESP)
This utilizes gaseous ions to charge particles which are
then moved through an electric field to be depositedonto charged collection plates.
ESP consists of two set of electrodes:
1. Collection Electrodes
rows of electrically grounded vertical parallel plates
2. Discharge Electrodes
wire electrodes centrally located.
The wires carry a unidirectional, negatively charged,
high voltage(20-100kV) current from an external
source.
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The applied high voltage generates a unidirectional,
non-uniform electric field whose magnitude is
greatest near the discharge electrode.
When that voltage is high enough, a blue luminous
glow, called a corona, is produced around them.
The corona is an indication of the generation of
negatively charged gas ions.
The gas close to the negative electrode is ionized upon
passing through the corona.
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The charged gas ions travel from the wires to the
grounded collection electrodes as result of the
strong electric field between them.
The electrostatic field then draws the particles to the
collector surface where they are deposited.
Collected particulate material is then removed by
rapping or washing of the plates.
Usually, a large number of these collectors are placed
in parallel in a single housing.
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The internal gas passages within a precipitator are
relatively open with small pressure drops and lower
energy costs to move the gas stream.
Collection Efficiency
High collection efficiencies are possible, but efficiencymay drastically change with changes in operating
parameters.
The efficiency is a function of gas flow rate and
precipitator size is given by Deutsch equation.
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Performance & Efficiency Parameters
Collection Efficiency(Deutsch equation)
= 1 - eVm.A/Q
where A = collecting electrode area
Q = volumetric gas flow rateVm = particle migration velocity
andDrift/migration velocity =
Where E = Applied voltage(V)
s = Distance between electrodes(m)d = Particle diameter(m)
g = Gas viscosity(kg/m.s)
p = Particle dielectric constant(1.52.4)
12 22.95 10 ( / )m
g
X p E s dV
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Limitations / Advantages / Problems
Large installation space required High efficiencies for small particles possible
Low pressure drops and air moving costs
High potential for ignition sources Re-entrainment, spark-over, back corona
problems
High temperature operation possible Susceptible to changes in moisture and
resistivity
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GASEOUS POLLUTANT CONTROL
ABSORPTION & WET SCRUBBING
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ABSORPTION & WET SCRUBBING
EQUIPMENT
The removal of gases and particulate matter by causing the
gaseous contamination to become dissolved into the
liquid stream and the solids to be entrained in the liquid.
The rate of gas transfer into the liquid is dependent upon
the solubility,
mass transfer mechanism, and
equilibrium concentration of the gas in solution.
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Gas collection efficiencies in the range of 99% are
possible.
The rate of particulate matter collection at constant
pressure drops is inversely proportional to
the aerodynamic mean dia. of the particulate matter andscrubber droplets.
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Performance & Efficiency Parameters
For gas collection, the maximum equilibrium concentration insolution is described by Henry's law:
[Cgas
] = (Hk) [C
liquid]
Where (Hk) is Henry's constant
[Cgas] is the concentration in the gas stream
[Cliquid] is the concentration in the liquid stream
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Limitations / Advantages / Problems
High pressure drops required
Internal plugging, corrosion, erosion
Increased need for internal inspection
Formation / precipitation of solids
Few internal moving parts
Reduced opportunity for gas ignition
Gas and liquid chemistry control important Increased relative velocity between scrubbing the
fluid and gas stream, increases efficiency for solids
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THANK YOU