ENVI ENG Particulate Emissions
Wastewater-to-Air Interface
- Typical Stages of Wastewater Treatment
- Preliminary → Primary → Secondary → (Tertiary/Polishing)
- Purpose: progressively reduce solids & organic loads before discharge or reuse.
- Relevance to air quality: aeration, stripping and sludge handling can release odorous/VOC emissions; therefore air-pollution devices are often co-designed with WWTP units.
- Shared Control Philosophy
- Whether treating water or air, engineers try to:
- Reduce pollutant load as early as possible (pretreatment).
- Combine simple, low-cost removal first (screens, cyclones).
- Follow with higher-efficiency or high-cost devices (baghouse, ESP, scrubbers, etc.).
Particulate Control Devices (Dry Phase)
- Cyclone or Centrifugal Collector
- Swirling gas imparts centrifugal force; particles migrate to wall, fall into hopper.
\text{Typical cut size } d_{50} \approx 10\,\mu\text{m}
- Advantages: no moving parts, high-temperature tolerance, low pressure drop.
- Limitation: mainly removes coarse particles; fine PM usually needs a polishing step.
- Multicyclone (Cluster of Small Cyclones)
- Many parallel small-diameter tubes ⇒ higher centrifugal acceleration.
- Widely used as pre-cleaner in cement & boiler industries.
- Still considered easier & cheaper than equivalent wet scrubber.
- Fabric Filter (Baghouse)
- Dirty gas passes through cloth; dust cake forms and becomes the primary filter.
- Cleaning: shaking, reverse air, or pulse-jet; transcript mentions “rapping-vibration of collection plates” (analogy with ESP).
- Designers often specify “cyclone + baghouse” tandem: cyclone protects bags from large/abrasive dust ⇒ longer bag life, smaller baghouse.
- Hopper
- Under every dry collector; serves as dust receiver.
- Must be air-tight to avoid re-entrainment.
Gas/Vapor → Liquid Phase Controls
- Wet Scrubbing Basics
- Pollutant gas contacts liquid (usually water) and is absorbed, condensed or chemically reacted.
- Example stated: VOC stream → scrubber (water or chemical) produces CO₂ + H_{2}O downstream (if followed by incineration).
- For NOₓ:
- NO/NO₂ sparingly soluble, but can be oxidised/reduced → more soluble forms.
- Transcript note: “Nitrogen gas → water → Ammonia” hints at selective catalytic/non-catalytic reduction (SCR/SNCR) where ammonia reacts with NOₓ.
- Disorption / Desorption
- Opposite of absorption: liberating a species from liquid to gas, often by heating or stripping with air/steam.
- Used when solvent is regenerated chemically or thermally.
Condensation (Pretreatment Device)
- Process Definition
- Convert gas/vapor → liquid by:
- Lowering temperature, and/or
- Raising pressure.
- Types
- Contact condenser: gas mixes directly with cold liquid.
- Surface condenser: gas is separated from coolant by a heat-transfer surface (e.g., shell-and-tube).
- Role in Air Pollution Control
- Reduces flowrate & organic load before expensive devices (absorber, adsorber, incinerator).
- Removal efficiency: 50–95% depending on design & vapor pressure of contaminant.
- Energy recovered as warm condensate can be reused.
Incineration / Combustion Controls
- Fundamental Reaction
- \text{Hydrocarbon} + O{2} \xrightarrow{\ \Delta\ } CO{2} + H_{2}O + \text{heat}
- Converts VOC, odorous sulfides, etc., to relatively innocuous products.
- Direct Combustion (Flares)
- Waste gas + air burn at nozzle; no residence chamber.
- EPA-measured destruction efficiency ≈ 98 %.
- Common for emergency releases or continuous vent gases with high heating value.
- Thermal Incinerator
- Burner flame heats a combustion chamber; residence time t \ge 0.5\,\text{s} at T \ge 760\,^{\circ}C typical.
- Achievable > 99 % destruction if time, temperature, turbulence, and oxygen (the “3 T + O” rule) are adequate.
- Catalytic Incinerator
- After the flame, gases pass through catalyst (noble metal or metal oxide).
- Lowers required temperature (≈ 250\text{–}400\,^{\circ}C) ⇒ fuel savings.
- Typical destruction efficiency > 95 %.
- Sensitive to poisons (Pb, S, halogens) ⇒ requires pretreatment.
Regulatory Lists & Key Pollutants
- US EPA Criteria Pollutants
- Particulate Matter (PM₁₀, PM₂.₅)
- Ground-Level Ozone (O_{3})
- Carbon Monoxide (CO)
- Lead (Pb)
- Nitrogen Dioxide (NO_{2})
- Sulfur Dioxide (SO_{2})
- Kyoto Protocol Greenhouse Gases
- CO{2},\ CH{4},\ N{2}O,\ \text{HFCs},\ \text{PFCs},\ SF{6}
- Philippine Clean Air Act Criteria (parallels EPA list)
- Total Suspended Particulates (TSP), PM₁₀
- Photochemical Oxidants (as O_{3})
- CO,\ Pb,\ NO{2},\ SO{2}
- Ozone-Depleting Substances (Montreal Protocol)
- Class I:
- Chlorofluorocarbons (CFCs), Halons, Carbon Tetrachloride, Methyl Chloroform, Methyl Bromide.
- Class II: Hydrochlorofluorocarbons (HCFCs).
- Precursors
- Photochemical smog: NO{x} + VOC in sunlight → O{3} & PANs.
- Acid deposition: SO{2},\ NO{x} → H{2}SO{4},\ HNO_{3} aerosol.
Sampling & Measurement of Particulates
- Sedimentation / Settling Devices
- Fallout jars, Petri dishes, coated trays capture large settling dust.
- Directional samplers: vertical adhesive papers or cylinders with petroleum jelly.
- Inertial & Centrifugal Samplers
- Miniature cyclones separate particles > 10\,\mu\text{m}.
- Electrostatic Precipitator (ESP) Samplers
- Platinum wire electrode ionizes air; particles migrate to collection surface.
- Automatic Tape Smoke Sampler
- Deposits soot on moving filter tape; gives time-resolved “dirtiness” index (not mass-accurate for TSP standard).
- High-Volume (Hi-Vol) Sampler
- Flow: 40–60 cfm through quartz/fiber filter (EPA reference).
- Gravimetric equation:
PM\,\text{concentration} = \frac{W{\text{after}} - W{\text{before}}}{Q_{\text{avg}} \times t}
where W in grams, Q in m^{3}\,\text{min}^{-1}, t in minutes.
- Impingers
- Force gas to change direction sharply.
- Wet impinger: high-speed jet into liquid ⇒ captures fine particles.
- Dry impinger (e.g., Andersen impactor stages): collects coarse particles on plates.
- Cascade Impactor
- Sequential nozzles of decreasing diameter; deposits size-segregated fractions on slides; useful for lung deposition studies.
- Nuclei Counter
- Air saturated & adiabatically expanded ⇒ supersaturation ⇒ droplets form on nuclei; optical count gives number of condensation nuclei (useful for fog & cloud studies).
- Pollen Sampler
- Petroleum-jelly-coated slide exposed 24 h; grains counted microscopically; assists allergen forecasting.
Additional Concepts & Connections
- Velocity Considerations
- Low gas velocity in cyclone ⇒ larger cut size (loses fine PM).
- High velocity ⇒ higher pressure drop & erosion; balance required.
- Load Reduction Strategy
- Condenser or cyclone frequently installed upstream of absorber/ESP/Baghouse to "protect" expensive units and reduce OPEX.
- Environmental & Ethical Context
- Regulatory compliance built on health-based standards (EPA, Philippine CAA).
- Engineers must weigh operating cost vs. public health benefit; e.g., catalytic incineration saves fuel but may require precious metals.
- Proper hopper sealing prevents secondary dust emissions, reflecting the hierarchy: prevent → control → dispose.
Key Equations & Quantities (Compilation)
- Centrifugal acceleration in cyclone:
a{c} = \frac{v{t}^{2}}{r} - Residence time for combustion:
t = \frac{V{\text{chamber}}}{Q{\text{gas}}} - Condenser heat duty (simplified):
Q = m{v} (h{v} - h_{l})
Quick Reference: Device Selection Guide
- Coarse PM (> 10\,\mu m): settling chamber, cyclone.
- Fine PM (1–10 µm): baghouse, wet scrubber, multicyclone, ESP.
- Sub-micron & fumes: ESP, fabric filter with membrane, HEPA.
- Gaseous organics: condenser (pre), adsorber, absorber, incinerator.
- NOₓ: SCR/SNCR (ammonia), wet scrubber with oxidant.
- Acid gases (SO₂, HCl): limestone spray tower, packed scrubber.