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AIR POLLUTION PREVENTION AND CONTROL Dr. Wesam Al Madhoun.
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Transcript of AIR POLLUTION PREVENTION AND CONTROL Dr. Wesam Al Madhoun.
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AIR POLLUTION PREVENTION AND CONTROL
Dr. Wesam Al Madhoun
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Pollution Prevention Strategies
• Pollution prevention [vs. control] offers important economic benefits and at the same time allows continued protection of the environment.
• While most pollution control strategies cost money, pollution prevention has saved many firms thousands of dollars in treatment and disposal costs.
• More importantly, pollution prevention should be viewed as a means to increase company productivity.
• By reducing the amount of raw materials that are wasted and disposed of; manufacturing processes become more efficient, resulting in cost savings to the company.
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• Pollution prevention should be the first consideration in
planning for processes that emit air contaminants.
• Undertaking pollution prevention practices may reduce
air emissions enough to allow a business or industry to
avoid classification as a major air emission source.
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What is Pollution Prevention?
• Pollution prevention is the elimination or prevention of wastes (air
emissions, water discharges, or solid/hazardous waste) at the
source. In other words, pollution prevention is eliminating wastes
before they are generated.
• Pollution prevention approaches can be applied to all pollution
generating activity: hazardous and nonhazardous, regulated and
unregulated. Pollution prevention does not include practices that
create new risks of concern.
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Pollution Prevention Act
In 1990, the US Congress established federal policy on
pollution prevention by passing the Pollution
Prevention Act. The Act states:
1. pollution should be prevented or reduced at the source
whenever feasible (i.e., source reduction),
2. pollution that cannot be prevented should be recycled
in an environmentally safe manner whenever feasible,
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3. pollution that cannot be prevented or recycled should
be treated in an environmentally safe manner
whenever feasible, and
4. disposal or other release into the environment should
be employed only as last resort and should be
conducted in an environmentally safe manner.
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The Pollution Prevention Act defines pollution prevention as
source reduction. Recycling, energy recovery, treatment and
disposal are not considered pollution prevention under the
Act.
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SOURCE REDUCTION
• Product Changes
• Designing and producing a product that has less environmental impact
• Changing the composition of a product so that less hazardous
chemicals are used in, and result from, production
• Using recycled materials in the product
• Reusing the generated scrap and excess raw materials back in the
process
• Minimizing product filler and packaging
• Producing goods and packaging reusable by the consumer
• Producing more durable products
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• Input Material Changes
• Material substitution Using a less hazardous or
toxic solvent for cleaning or as coating
• Purchasing raw materials that are free of trace
quantities of hazardous or toxic impurities
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Equipment and Process Modifications
•Changing the production process or flow of materials through the
process.
•Replacing or modifying the process equipment, piping or layout.
•Using automation.
•Changing process operating conditions such as flow rates,
temperatures, pressures and residence times.
•Implementing new technologies
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Good Operating Practices
• Instituting management and personnel programs such as employee training or employee incentive programs that encourage employees to reduce waste.
• Performing good material handling and inventory control practices that reduce loss of materials due to mishandling, expired shelf life, or improper storage.
• Preventing loss of materials from equipment leaks and spills.
• Segregating hazardous waste from non-hazardous waste to reduce the volume of hazardous waste disposed.
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• Using standard operating procedures for process operation and maintenance tasks
• Performing preventative maintenance checks to avoid unexpected problems with equipment.
• Turning off equipment when not in use.
• Improving or increasing insulation on heating or cooling lines.
• Environmentally Sound Reuse and Recycling
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Control of Gaseous Pollutants
• Absorption
• Adsorption
• Oxidation
• Reduction
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Absorption
Primary application: inorganic gasesExample: SO2
Mass transfer from gas to liquid
Contaminant is dissolved in liquid
Liquid must be treated
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Adsorption
Primary application: organic gasesExample: trichloroethylene
Mass transfer from gas to solid
Contaminant is ‘bound’ to solid
Adsorbent may be regenerated
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Common Adsorbents
Activated carbon
Silica gel
Activated alumina
Zeolites (molecular sieves)
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Oxidation
• Thermal Oxidation
• Catalytic Oxidation
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• A thermal oxidizer (or thermal oxidiser) is a process unit for air pollution
control in many chemical plants that decomposes hazardous gases at a high
temperature and releases them into the atmosphere.
• Thermal Oxidizers are typically used to destroy Hazardous Air Pollutants
(HAPs) and Volatile Organic Compounds (VOCs) from industrial air
streams.
• These pollutants are generally hydrocarbon based and when destroyed via
thermal combustion they are chemically changed to form CO2 and H2O.
•
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Thermal Oxidation
Application: organic gases
Autogenous gases = 7 MJ/kg (heat value)
Operating temperatures: 700 - 1300 oC
Efficiency = 95 - 99%
By-products must not be more hazardous
Heat recovery is economical necessity
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• Catalytic oxidation is a relatively recently applied alternative for the treatment of VOCs in air streams resulting from remedial operations.
• The addition of a catalyst accelerates the rate of oxidation by adsorbing the oxygen and the contaminant on the catalyst surface where they react to form carbon dioxide, water, and hydrochloric gas.
• The catalyst enables the oxidation reaction to occur at much lower temperatures than required by a conventional thermal oxidation
Catalytic Oxidation
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Catalytic Oxidation
Application: organic gases
Non-autogenous gases < 7 MJ/kg
Operating temperatures: 250 - 425 oC
Efficiency = 90 - 98%
Catalyst may be poisoned
Heat recovery is not normal
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Selective Catalytic Reduction(SCR)
Application: NOx control
Ammonia is reducing agent injected into exhaust
NOx is reduced to N2 in a separate reactor containing catalyst
Reactions:
4NO + 4NH3 + O2 --> 4N2 + 6H2O
2NO2 + 4NH3 + O2 --> 3N2 + 6H2O
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Control of Particulate Pollutants
• Spray chamber
• Cyclone
• Bag house
• Venturi
• Electrostatic Precipitator (ESP)
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Spray Chamber
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Spray Chamber
Primary collection mechanism:
Inertial impaction of particle into water droplet
Efficiency:
< 1% for < 1 um diameter
>90% for > 5 um diameter
Pressure drop: 0.5 to 1.5 cm of H2O
Water droplet size range: 50 - 200 um
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Spray Chamber
Applications:
1. Sticky, wet corrosive or liquid particles
Examples: chrome plating bath
paint booth over spray
2. Explosive or combustible particles
3. Simultaneous particle/gas removal
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Cyclone
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Cyclone(Multi-clones for high gas volumes)
Primary collection mechanism:
Centrifugal force carries particle to wall
Efficiency:
<50% for <1 um diameter
>95% for >5 um diameter
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Cyclone(Multi-clones for high gas volumes)
Pressure drop: 8-12 cm of H2O
Applications:
1. Dry particles
Examples: fly ash pre-cleaner
saw dust
2. Liquid particles
Examples: following venturi
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Bag House
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Bag HouseParticle Collection Mechanisms
Screening Impaction
+
-
Electrostatic
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Bag House
Efficiency:
>99.5% for <1 um diameter
>99.8% for >5 um diameter
Fabric filter materials:
1. Natural fibers (cotton & wool)
Temperature limit: 80 oC
2. Synthetics (acetates, acrylics, etc.) Temperature limit: 90 oC
3. Fiberglass
Temperature limit: 260 oC
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Bag House
Bag dimensions:
15 to 30 cm diameter
~10 m in length
Pressure drop: 10-15 cm of H2O
Cleaning:
1. Shaker
2. Reverse air
3. Pulse jet
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Bag House
Applications:
Dry collection
Fly ash
Grain dust
Fertilizer
May be combined with dry adsorption media to control gaseous emission (e.g. SO2)
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Venturi
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Venturi
Primary collection mechanism:
Inertial impaction of particle into water droplet
Water droplet size: 50 to 100 um
Water drop and collected particle are removed by cyclone
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Venturi
Efficiency:
>98% for >1 um diameter
>99.9% for > 5 um diameter
Very high pressure drop: 60 to 120 cm of H2O
Liquid/gas ratios: 1.4 - 32 gal/1000 ft3 of gas
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Venturi
Applications:
Phosphoric acid mist
Open hearth steel (metal fume)
Ferro-silicon furnace
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Electrostatic Precipitator (ESP)
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ESP Tube (a) and Plate (b) collectors
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ESP Collection Mechanism
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Electrostatic Precipitator (ESP)
Efficiency:
>95% for >1 um diameter
>99.5% for > 5 um diameter
Pressure drop: 0.5 to 1.5 cm of H2O
Voltage: 20 to 100 kV dc
Plate spacing: 30 cm
Plate dimensions: 10-12 m high x 8-10 m long
Gas velocity: 1 to 1.5 m/s
Cleaning: rapping plates
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Electrostatic Precipitator (ESP)
Applications (non-explosive):
1. Fly ash
2. Cement dust
3. Iron/steel sinter
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Flue Gas Desulfurization(FGD)
Predominant Processes (all non-regenerative):
1. Limestone wet scrubbing
2. Lime wet scrubbing
3. Lime spray drying
Typical scrubbers: venturi, packed bed and plate towers and spray towers
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Flue Gas Desulfurization(FGD)
Spray dryer systems include a spray dryer absorber and a particle-collection system (either a bag house or an ESP)
In 1990 the average design efficiency for new and retrofit systems was 82% and 76% respectively
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Flue Gas Desulfurization(FGD)
Overall reactions:
Limestone: SO2 + CaCO3 --> CaSO3 + CO2
Lime: SO2 + Ca(OH)2 --> CaSO3 + H2O