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Welcome to
Electrostatic Precipitator
Plant services
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EFFECTS OF AIR POLLUTION
•GENERAL– VISIBILITY REDUCTION DUE TO SCATTERING OF LIGHT
FROM SURFACES OF AIR BORNE PARTICLES
–
MATERIAL DAMAGE– AGRICULTURAL DAMAGE DUE TO ASH DEPOSITION
• LOSS AND REDUCTION OF GREEN PLANT PIGMENT
CALLED CHLOROPHYLL RESULTING IN YELLOWING AND
EVEN DROPPING OF LEAVES.
– DAMAGE TO BUILDINGS, MONUMENTS OF MARBLE
ETC.
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EFFECTS OF AIR POLLUTION
• HUMAN HEALTH
– OCCUPATIONAL SKIN DECEASE
– AFFECTS LUNGS - SILICOSIS FOR FOUNDRY WORKMEN
– RESPIRATORY CONDITION DUE TO TOXIC AGENTS
• ACUTE CONJUNCTIONS DUE TO CHEMICAL DUSTS, FUMES
AND GASES
– DISORDER DUE TO PHYSICAL AGENTS - ENVIRONMENTAL
HEAT OR LOW TEMPERATURE
– EYE IRRITATION, COUGH AND BREATHLESSNESS
– FORMATION OF CARBOXYL HEMOGLOBIN WHICH
PREVENTS O2 CARRIAGE BY BLOOD
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GROWTH OF PROBLEMS OF AIR POLLUTION
• Rapid economic growth
•
Rapid industrialization and urbanization• Increased industrial production
• Population explosion
• Growth in demand for power
• Increase in requirement for thermal power plants
• More number of old coal based power plants
designed for high emission & low ash content coal
• High ash content or deterioration in quality of coal
reserve
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TYPES OF DUST COLLECTING EQUIPMENTS
Sl.NO. Type of Dustcollectors
Pressure
dropmmWc
Collection
effieicny,%
Remarks
1. Gravity Settling
chamber
25-30 30 to 40 Less efficiency, more
space required andnot suitable for powerplant
2. Inertial Collectors Impact
Centrifugal(cyclones)
30 – 40
60-80
30 – 40
75 to 80
Not for power plant
Were widely used inpower plants butcan not satisfy thepresent daypollution controlrequirement
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Sl.NO.
Type of Dustcollectors
Pressuredrop
mmWc
Collectioneffieicny,
%
Remarks
3. Scrubbers(wet) 50 to 60 80 to 90 Used mainly in procesindustries and can not
satisfy the pollutioncontrol requirement
4. Electrostaticprecipitators
15-25 99.99 Can meet any efficiencand mostly used in all
power plants.5 Fabric Filter 125 to150
99.99 Can meet any efficiencand used many poweplants abroad. Gainingmomentum in Indian
Power plants also.
TYPES OF DUST COLLECTING EQUIPMENTS
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PURPOSE OF POLLUTION CONTROL EQUIPMENT
•Recovery of material for economic reasons – Pulp and Paper Industries (Sodium Sulphate)
• Removal of abrasive material in the dust to
reduce wear and tear of the Fan components
• Removal of objectionable matter in the dust
– NO2 and SO2
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ADVANTAGES OF ELECTROSTATIC PRECIPITATORS
•
Very high collection efficiency• Low pressure drop
• capacity to collect sub-micron particles
• Robust construction - Longer life
• Less maintenance
•
Adaptability
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ELECTROSTATIC PRECIPITATOR PRINCIPLE
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ELECTROSTATIC PRECIPITATOR WORKING PRINCIPLE
The precipitation process involves 4 main functions
• Corona generation
• Particle charging
• Particle collection
• Removal of particles
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ESP - CORONA GENERATION
• Due to the ionisation of gas molecules, + ve ions, -ve ions and freeelectrons are generated.
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CORONA DISCHARGE IN SPIRAL ELECTRODE
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ESP - PARTICLE CHARGING
• The -ve charges of ions and free electrons travel towards +ve electrodeand the +ve charges of ions travel towards -ve electrodes.
• When -ve ions travel towards +ve electrodes, the -ve charges get
attached to the dust particles and thus the dust particles areelectrically charged,
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ESP - PARTICLE COLLECTION
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ESP - REMOVAL OF PARTICLE
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ESP SIZING THEORY
DEUTSCH - ANDERSON EQUATION
Collection Efficiency = 1 - e - w. SCA
where,
w = Migration velocity
SCA = Specific Collecting Area
• Migration Velocity – The velocity which the dust particle travel towards the collecting electrode
under the influence of electric field.
• Specific collecting area
– Amount of collecting area required to be provided to collect dust in gasflow rate of 1 m3/s.
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DEFINITIONS
• Flue gas velocity, m/s = Flue gas flow in m3
ESP effective cross section m2
• Aspect ratio = Effective length of ESP
Collecting electrode height
• Treatment time, sec = Effective length of ESP in m
Flue gas velocity in m/s
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DEFINITIONS
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EFFECT OF VARIOUS PARAMETERS
Gas velocity
• velocity is decided by the gas flow and collection efficiencyrequired
•
Higher the gas velocity, higher the carryover of dustparticles without collection - Re-entertainment
• Very poor velocity alters the flow distribution and effectssettling of dust particles
•
optimum velocity depends upon the application willimprove the performance.
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EFFECT OF VARIOUS PARAMETERS
Aspect ratio
• During the rapping, the falling of dust particle take a trajectoryform
•
Lower the aspect ratio, the trajectory dust travel along with gasflow without falling in to hoppers - Leads to re-entrainmentloss.
• Higher the ratio, performance will be good
•
optimum aspect ratio depends on allowable velocity, requiredcollection efficiency and available space.
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EFFECT OF VARIOUS PARAMETERS
Treatment time
• Time available for capturing the dust particle
• more treatment time at reasonable velocity improves the
collection efficiency• Probability of capturing the re-entrained partilces improves
with time.
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ENVIRONMENTAL REGULATIONS IN INDIA
Prior to 1984
• 1974 – water act• 1977 – water cess act
• 1981 – air act
The cost of compliance was more than that of non-compliance:
• 1986 – Environmental Protection Act
comprehensive act with ‘command & control’
• Future trend is to internalize the environmentalimprovement cost
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REVISED EMISSION STANDARD(GAZETTE NOTIFICATION BY MINISTRY OF E&F DATED 19 05 93)
• SUSPENDED PARTICULATE MATTER (SPM) : < 150 mg/Nm3
•
STANDARD ALSO STATES THAT• FOR POWER PLANTS
•CAPACITY LESS THAN 62.5 MW AND
COMMISSIONED BEFORE 01 01 1982 : 350 mg/Nm3
• FOR CEMENT PLANTS (TOTAL EMISSIONS)
• CAPACITY LESS THAN 200 TPD : 400 mg/Nm3
• CAPACITY MORE THAN 200 TPD : 250 mg/Nm3
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ENVIRONMENTAL REGULATIONS
– TODAY’S WORLD
World Bank’s ‘proposed guide lines’
• For new thermal power plants (TPP) forcapacities ≥ 50 MW
• Pollution control at project formulation levelitself
• Site specific emission guide line
• Propose standard of 50 mg/Nm3• Aided projects are to abide by this
• Further implication on technical, economic &
institutional
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Emission of various pollutants under the
business-as-usual scenarioProjection
0.1582.82434.022.0736.22011
0.1252.19338.019.6605.52006
0.0891.75259.117.9511.02001
0.0491.340.3016.162428.01996
SOXNOXSPMCOCO2
POLLUTANTS (MT)YEAR
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COMPARISON OF PARTICULATE EMISSION
NORMS IN OTHER COUNTRIES
150India
4356Sweden
194250Australia
3950Europian community3950Germany
2836USA
ppmMg/Nm3Country
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DESIGN DATA REQUIRED FOR ESP
• Application
• Process data
• Gas composition• Gas pressure
• Gas moisture
• Dust composition
• Particle size distribution
• Basic design data
• Gas flow rate
•
Gas temperature• Inlet dust concentration
• Environmental data
• Outlet emission
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FACTORSW CONSIDERED FOR ESP SELECTION
• Gas flow
• Gas temperature
• Inlet dust concentration
•Required outlet emission
• Required collection efficiency
• Moisture in gas
• Sulphur content in coal
• Ash resisitivity• Particle size distribution
• No. of ESPs per boiler
• Minimum number of fields required
• Minimum Specific collecting area• Maximum gas velocity
• Minimum aspect ratio
• Maximum area connected to one TR set
• Collecting electrode spacing
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ESP DESIGN CONSIDERATIONS
HIGH INLET DUST REQUIRES LARGER ESP
EMISSION VS ESP EFFICIENCY FOR
DIFFERENT DUST BURDEN
99.25
99.5
99.75
100
25 50 75 100 125 150
EMISSION REQUIREMENT-
mg/Nm3
E F F
I C I E N C Y R E Q U I R E M
E N T -
20g/Nm3
40 g/Nm3
60 g/Nm3
80 g/Nm3
100 g/Nm3
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ESP DESIGN CONSIDERATIONS
ESP COLLECTION EFFICIENCY VS SIZE
0
1
2
3
4
5
6
7
8
9
90 91 92 93 94 95 96 97 98 99 100
COLLECTION EFFICIENCY - %
C
O M P A R A T I V E E
S P S I Z
BASE : ESP SIZE FOR 90% = 1
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ELECTROSTATIC PRECIPITATOR
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ELECTROSTATIC PRECIPITATOR