Specialized skill for air pollution control equipment selection and design including scrubbers, baghouses, ESPs, oxidizers, and BACT/LAER determination.
Scanned 9/2/2026
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---
name: air-pollution-control
description: Specialized skill for air pollution control equipment selection and design including scrubbers, baghouses, ESPs, oxidizers, and BACT/LAER determination.
allowed-tools: Read, Grep, Write, Bash, Edit, Glob
category: Air Quality Management
backlog-id: SK-007
metadata:
author: babysitter-sdk
version: "1.0.0"
graph:
domains: [domain:environmental-engineering]
skillAreas: [skill-area:data-analysis, skill-area:statistical-analysis, skill-area:geospatial-data-analysis]
workflows: [workflow:experiment-design]
roles: [role:research-engineer]
---
# Air Pollution Control Design Skill
Air pollution control equipment selection and design for industrial emission reduction.
## Purpose
This skill provides comprehensive capabilities for designing air pollution control systems, including technology selection, equipment sizing, efficiency calculations, and regulatory compliance demonstration (BACT/LAER/MACT).
## Capabilities
### Scrubber Design
- Wet scrubber technology selection
- Packed tower design and sizing
- Spray tower configuration
- Venturi scrubber design
- Pressure drop calculations
- Liquid-to-gas ratio optimization
- Chemical dosing requirements
### Baghouse and Fabric Filter Sizing
- Filter media selection
- Air-to-cloth ratio determination
- Compartmentalization design
- Pulse-jet vs reverse-air cleaning
- Pressure drop estimation
- Bag life prediction
- Hopper sizing
### Electrostatic Precipitator Design
- Collection efficiency calculation
- Specific Collection Area (SCA) determination
- Plate spacing and configuration
- Electrical field strength
- Rapping system design
- Resistivity considerations
- Power supply sizing
### Thermal and Catalytic Oxidizer Specification
- Destruction efficiency requirements
- Temperature and residence time
- Heat recovery options (regenerative, recuperative)
- Catalyst selection for catalytic oxidizers
- Auxiliary fuel requirements
- Turndown capabilities
### Carbon Adsorption System Design
- Activated carbon selection
- Adsorption capacity calculations
- Breakthrough time estimation
- Bed sizing
- Regeneration system design
- Carbon replacement frequency
### Control Efficiency Calculations
- Outlet emission rate determination
- Removal efficiency verification
- Stack testing correlation
- Continuous monitoring requirements
### Pressure Drop and Energy Analysis
- System pressure drop calculation
- Fan power requirements
- Operating cost estimation
- Energy optimization opportunities
### BACT/LAER/MACT Determination
- Control technology identification
- Cost-effectiveness analysis
- Technical feasibility evaluation
- Regulatory database research
- Top-down BACT analysis
## Prerequisites
### Installation
```bash
pip install numpy scipy pandas matplotlib
```
### Optional Dependencies
```bash
# For chemical property lookup
pip install chemicals thermo
# For visualization
pip install plotly
```
## Usage Patterns
### Baghouse Design
```python
import numpy as np
from dataclasses import dataclass
from typing import Dict, List, Optional
@dataclass
class GasStreamData:
"""Gas stream characteristics"""
flow_rate_acfm: float
temperature_f: float
moisture_pct: float
particulate_loading_gr_acf: float
particle_size_micron: float
gas_composition: Dict[str, float] = None
@dataclass
class BaghouseDesign:
"""Baghouse design parameters"""
filter_media: str
bag_diameter_in: float
bag_length_ft: float
air_to_cloth_ratio: float
cleaning_type: str # 'pulse_jet', 'reverse_air', 'shaker'
class BaghouseCalculator:
"""Pulse-jet baghouse sizing calculations"""
# Recommended air-to-cloth ratios (acfm/ft2) by application
AC_RATIOS = {
'cement': {'gross': 4.0, 'net': 3.5},
'coal': {'gross': 6.0, 'net': 5.0},
'foundry': {'gross': 4.5, 'net': 3.5},
'steel': {'gross': 5.0, 'net': 4.0},
'chemical': {'gross': 5.5, 'net': 4.5},
'pharmaceutical': {'gross': 3.5, 'net': 3.0},
'general': {'gross': 5.0, 'net': 4.0}
}
# Filter media properties
MEDIA_PROPERTIES = {
'polyester': {'max_temp_f': 275, 'cost_factor': 1.0, 'acid_resist': 'good'},
'polypropylene': {'max_temp_f': 200, 'cost_factor': 0.9, 'acid_resist': 'excellent'},
'nomex': {'max_temp_f': 400, 'cost_factor': 3.0, 'acid_resist': 'good'},
'fiberglass': {'max_temp_f': 500, 'cost_factor': 2.5, 'acid_resist': 'excellent'},
'ptfe': {'max_temp_f': 500, 'cost_factor': 8.0, 'acid_resist': 'excellent'},
'p84': {'max_temp_f': 500, 'cost_factor': 5.0, 'acid_resist': 'good'}
}
def select_filter_media(self, gas: GasStreamData) -> str:
"""Select appropriate filter media based on gas conditions"""
temp = gas.temperature_f
suitable = []
for media, props in self.MEDIA_PROPERTIES.items():
if props['max_temp_f'] >= temp:
suitable.append((media, props))
# Return lowest cost suitable media
suitable.sort(key=lambda x: x[1]['cost_factor'])
return suitable[0][0] if suitable else 'ptfe'
def calculate_filter_area(self, gas: GasStreamData,
application: str = 'general',
use_net_ratio: bool = True) -> Dict:
"""Calculate required filter area"""
ratios = self.AC_RATIOS.get(application, self.AC_RATIOS['general'])
ac_ratio = ratios['net'] if use_net_ratio else ratios['gross']
filter_area = gas.flow_rate_acfm / ac_ratio
return {
'gas_flow_acfm': gas.flow_rate_acfm,
'air_to_cloth_ratio': ac_ratio,
'filter_area_sqft': filter_area
}
def size_baghouse(self, gas: GasStreamData,
bag_diameter_in: float = 6.0,
bag_length_ft: float = 10.0,
application: str = 'general') -> Dict:
"""Size complete baghouse system"""
# Filter media selection
media = self.select_filter_media(gas)
# Calculate filter area
area_calc = self.calculate_filter_area(gas, application)
required_area = area_calc['filter_area_sqft']
# Bag area calculation
bag_area = np.pi * (bag_diameter_in / 12) * bag_length_ft # sq ft per bag
# Number of bags
num_bags = np.ceil(required_area / bag_area)
# Compartments (typically 8-16 bags per row, 2-4 rows per compartment)
bags_per_compartment = 32 # typical
num_compartments = np.ceil(num_bags / bags_per_compartment)
# Pressure drop estimate (typical for pulse-jet)
dp_filter = 2.5 # inches w.c. for clean filter
dp_tubesheet = 0.5
dp_inlet_outlet = 1.0
total_dp = dp_filter + dp_tubesheet + dp_inlet_outlet
# Hopper sizing (4:1 turndown, 8-hour storage)
dust_rate_lb_hr = gas.particulate_loading_gr_acf * gas.flow_rate_acfm * 60 / 7000
hopper_volume = dust_rate_lb_hr * 8 / 50 # 50 lb/cf bulk density
return {
'filter_media': media,
'required_filter_area_sqft': required_area,
'bag_diameter_in': bag_diameter_in,
'bag_length_ft': bag_length_ft,
'area_per_bag_sqft': bag_area,
'total_bags': int(num_bags),
'num_compartments': int(num_compartments),
'air_to_cloth_gross': gas.flow_rate_acfm / (num_bags * bag_area),
'pressure_drop_in_wc': total_dp,
'dust_rate_lb_hr': dust_rate_lb_hr,
'hopper_volume_cf': hopper_volume,
'max_temp_f': self.MEDIA_PROPERTIES[media]['max_temp_f']
}
# Example usage
gas = GasStreamData(
flow_rate_acfm=50000,
temperature_f=350,
moisture_pct=8,
particulate_loading_gr_acf=2.0,
particle_size_micron=5
)
calculator = BaghouseCalculator()
design = calculator.size_baghouse(gas, application='cement')
print(f"Filter media: {design['filter_media']}")
print(f"Total bags: {design['total_bags']}")
print(f"Compartments: {design['num_compartments']}")
print(f"A/C ratio: {design['air_to_cloth_gross']:.2f} acfm/sqft")
print(f"Pressure drop: {design['pressure_drop_in_wc']:.1f} in w.c.")
```
### Wet Scrubber Design
```python
class WetScrubberDesign:
"""Wet scrubber design calculations"""
def packed_tower_sizing(self, gas_flow_acfm: float,
pollutant: str,
inlet_conc_ppm: float,
outlet_conc_ppm: float,
scrubbing_liquid: str = 'water') -> Dict:
"""Size packed tower for gas absorption"""
# Removal efficiency
efficiency = (inlet_conc_ppm - outlet_conc_ppm) / inlet_conc_ppm
# Gas velocity (typical range 3-6 ft/s for packed towers)
gas_velocity_fps = 4.5
# Cross-sectional area
area_sqft = (gas_flow_acfm / 60) / gas_velocity_fps
# Diameter
diameter_ft = np.sqrt(4 * area_sqft / np.pi)
# Height based on NTU (simplified)
ntu = -np.log(1 - efficiency) # Number of transfer units
htu = 2.5 # Height of transfer unit (ft) - typical for 2" packing
packing_height = ntu * htu
# L/G ratio (liquid to gas)
lg_ratio = 10 # gpm per 1000 acfm typical
# Liquid flow rate
liquid_flow_gpm = gas_flow_acfm * lg_ratio / 1000
# Pressure drop (1-2 in w.c. per ft of packing typical)
pressure_drop = packing_height * 1.5
return {
'diameter_ft': diameter_ft,
'packing_height_ft': packing_height,
'total_height_ft': packing_height * 1.5, # Add for internals
'cross_section_sqft': area_sqft,
'gas_velocity_fps': gas_velocity_fps,
'liquid_flow_gpm': liquid_flow_gpm,
'lg_ratio_gpm_per_kacfm': lg_ratio,
'pressure_drop_in_wc': pressure_drop,
'removal_efficiency_pct': efficiency * 100,
'ntu': ntu
}
def venturi_scrubber_sizing(self, gas_flow_acfm: float,
particulate_loading_gr_acf: float,
target_efficiency_pct: float) -> Dict:
"""Size venturi scrubber for particulate removal"""
# Pressure drop vs efficiency correlation (Johnstone equation)
# Efficiency increases with pressure drop
# For 99% efficiency, typically need 30-50 in w.c.
if target_efficiency_pct >= 99:
pressure_drop = 50
elif target_efficiency_pct >= 95:
pressure_drop = 30
elif target_efficiency_pct >= 90:
pressure_drop = 20
else:
pressure_drop = 10
# L/G ratio (higher for higher efficiency)
lg_ratio = 8 + (target_efficiency_pct - 90) * 0.2
# Throat velocity (typically 12,000-24,000 fpm)
throat_velocity = 15000 # fpm
# Throat area
throat_area = gas_flow_acfm / throat_velocity
# Liquid flow
liquid_flow = gas_flow_acfm * lg_ratio / 1000
return {
'throat_area_sqft': throat_area,
'throat_velocity_fpm': throat_velocity,
'pressure_drop_in_wc': pressure_drop,
'liquid_flow_gpm': liquid_flow,
'lg_ratio': lg_ratio,
'expected_efficiency_pct': target_efficiency_pct
}
# Example usage
scrubber = WetScrubberDesign()
# Packed tower for SO2 removal
packed = scrubber.packed_tower_sizing(
gas_flow_acfm=30000,
pollutant='SO2',
inlet_conc_ppm=1000,
outlet_conc_ppm=50
)
print(f"Packed tower diameter: {packed['diameter_ft']:.1f} ft")
print(f"Packing height: {packed['packing_height_ft']:.1f} ft")
print(f"Removal efficiency: {packed['removal_efficiency_pct']:.1f}%")
# Venturi for particulates
venturi = scrubber.venturi_scrubber_sizing(
gas_flow_acfm=30000,
particulate_loading_gr_acf=5.0,
target_efficiency_pct=95
)
print(f"\nVenturi pressure drop: {venturi['pressure_drop_in_wc']} in w.c.")
print(f"Liquid flow: {venturi['liquid_flow_gpm']:.0f} gpm")
```
### BACT Analysis
```python
class BACTAnalysis:
"""Best Available Control Technology analysis"""
# Control technology database (simplified)
CONTROL_TECHNOLOGIES = {
'PM': [
{'name': 'Baghouse', 'efficiency': 99.9, 'cost_per_ton': 500},
{'name': 'ESP', 'efficiency': 99.5, 'cost_per_ton': 400},
{'name': 'Cyclone', 'efficiency': 90, 'cost_per_ton': 100},
{'name': 'Wet Scrubber', 'efficiency': 95, 'cost_per_ton': 600}
],
'SO2': [
{'name': 'Wet FGD', 'efficiency': 98, 'cost_per_ton': 800},
{'name': 'Dry FGD', 'efficiency': 95, 'cost_per_ton': 600},
{'name': 'SDA', 'efficiency': 92, 'cost_per_ton': 500}
],
'NOx': [
{'name': 'SCR', 'efficiency': 90, 'cost_per_ton': 2000},
{'name': 'SNCR', 'efficiency': 60, 'cost_per_ton': 500},
{'name': 'Low-NOx Burner', 'efficiency': 50, 'cost_per_ton': 200}
],
'VOC': [
{'name': 'RTO', 'efficiency': 99, 'cost_per_ton': 3000},
{'name': 'Catalytic Oxidizer', 'efficiency': 98, 'cost_per_ton': 2500},
{'name': 'Carbon Adsorption', 'efficiency': 95, 'cost_per_ton': 1500},
{'name': 'Condenser', 'efficiency': 85, 'cost_per_ton': 800}
]
}
def top_down_bact(self, pollutant: str, uncontrolled_tpy: float,
cost_threshold: float = 15000) -> List[Dict]:
"""Perform top-down BACT analysis
Args:
pollutant: Pollutant type (PM, SO2, NOx, VOC)
uncontrolled_tpy: Uncontrolled emissions (tons per year)
cost_threshold: Maximum acceptable cost ($/ton removed)
"""
technologies = self.CONTROL_TECHNOLOGIES.get(pollutant, [])
# Sort by efficiency (highest first) - top-down approach
technologies = sorted(technologies, key=lambda x: x['efficiency'], reverse=True)
results = []
for tech in technologies:
tons_removed = uncontrolled_tpy * tech['efficiency'] / 100
controlled_emissions = uncontrolled_tpy - tons_removed
annual_cost = tech['cost_per_ton'] * tons_removed
cost_effectiveness = tech['cost_per_ton']
is_feasible = cost_effectiveness <= cost_threshold
results.append({
'technology': tech['name'],
'efficiency_pct': tech['efficiency'],
'controlled_emissions_tpy': controlled_emissions,
'tons_removed_tpy': tons_removed,
'annual_cost': annual_cost,
'cost_effectiveness': cost_effectiveness,
'is_cost_effective': is_feasible,
'bact_candidate': is_feasible
})
if is_feasible:
break # First cost-effective option is BACT
return results
def generate_bact_report(self, pollutant: str,
uncontrolled_tpy: float) -> str:
"""Generate BACT determination report"""
analysis = self.top_down_bact(pollutant, uncontrolled_tpy)
report = f"""
BACT DETERMINATION - {pollutant}
================================
Uncontrolled Emissions: {uncontrolled_tpy:.1f} tpy
TOP-DOWN ANALYSIS:
"""
for i, tech in enumerate(analysis, 1):
status = "BACT SELECTED" if tech['bact_candidate'] else \
"Eliminated - Cost" if not tech['is_cost_effective'] else "Evaluated"
report += f"""
Step {i}: {tech['technology']}
Control Efficiency: {tech['efficiency_pct']}%
Controlled Emissions: {tech['controlled_emissions_tpy']:.2f} tpy
Cost Effectiveness: ${tech['cost_effectiveness']:,.0f}/ton
Status: {status}
"""
# Find BACT
bact = next((t for t in analysis if t['bact_candidate']), None)
if bact:
report += f"""
BACT DETERMINATION:
Selected Technology: {bact['technology']}
Emission Limit: {bact['controlled_emissions_tpy']:.2f} tpy
Control Efficiency: {bact['efficiency_pct']}%
"""
return report
# Example usage
bact = BACTAnalysis()
report = bact.generate_bact_report('NOx', uncontrolled_tpy=100)
print(report)
# VOC BACT
voc_analysis = bact.top_down_bact('VOC', uncontrolled_tpy=50)
for tech in voc_analysis:
print(f"{tech['technology']}: {tech['efficiency_pct']}% - "
f"${tech['cost_effectiveness']}/ton - "
f"{'BACT' if tech['bact_candidate'] else 'Eliminated'}")
```
## Usage Guidelines
### When to Use This Skill
- Air pollution control system design
- Permit application preparation
- BACT/LAER/MACT determinations
- Control equipment optimization
- Emission reduction projects
### Best Practices
1. **Characterize emissions thoroughly** before design
2. **Consider multiple control options** for BACT
3. **Account for variable operating conditions** in sizing
4. **Include maintenance access** in design
5. **Design for turndown** when loads vary
6. **Plan for monitoring** to verify performance
### Process Integration
- AQ-002: Air Pollution Control System Design (all phases)
- AQ-001: Air Permit Application Development (BACT determination)
## Dependencies
- numpy: Numerical calculations
- scipy: Engineering correlations
## References
- EPA Air Pollution Control Technology Fact Sheets
- OAQPS Control Cost Manual
- EPA RACT/BACT/LAER Clearinghouse
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