1. Overview & Applications
Atmospheric dispersion modeling predicts how airborne pollutants travel and dilute after being released from a source. For midstream oil and gas facilities, dispersion analysis is essential for stack height design, permit applications, emergency response planning, and demonstrating compliance with ambient air quality standards.
Common Midstream Applications
| Application | Source Types | Key Pollutants |
|---|---|---|
| Compressor Station Permitting | Engine exhaust stacks, fugitive emissions | NOx, CO, VOC, PM, formaldehyde |
| Amine/Glycol Unit Vents | Regenerator still columns, flash tanks | H2S, BTEX, CH4, VOC |
| Flare Stack Siting | Elevated and ground flares | SO2, NOx, CO, incomplete combustion products |
| Emergency Release Analysis | Relief valves, blowdown stacks | H2S, SO2, hydrocarbons |
| Tank Battery Emissions | Storage tank vents, loading operations | VOC, HAPs, CH4 |
| PSD/NSR Permit Applications | All facility sources combined | All criteria pollutants |
Why Dispersion Modeling Matters
Dispersion modeling serves several critical purposes in midstream engineering:
- Stack height determination: Ensures pollutant concentrations at ground level do not exceed ambient standards
- Facility siting: Establishes safe distances between emission sources and receptors (residences, workplaces, public areas)
- Permit compliance: Demonstrates that facility emissions will not cause or contribute to NAAQS violations
- Emergency planning: Predicts toxic gas concentrations during accidental releases (H2S, SO2) for evacuation zone planning
- Equipment design: Sizes stacks, selects flare heights, and determines the need for emission controls
2. The Gaussian Plume Model
The Gaussian plume model is the most widely used method for estimating pollutant concentrations from point sources. Developed from work by Sutton (1932), Pasquill (1961), and Gifford (1961), it assumes that the concentration distribution in both the crosswind (y) and vertical (z) directions follows a Gaussian (bell-curve) distribution.
Diagram: Gaussian plume from an elevated stack showing coordinate system, sigma-y (lateral) and sigma-z (vertical) spread, effective stack height, and ground reflection
The General Equation
The steady-state Gaussian plume equation for a continuous point source with ground reflection is:
Key Assumptions
- Steady-state conditions: Emission rate, wind speed, and atmospheric stability are constant over the period of interest
- Uniform wind: Wind direction and speed do not vary with height within the plume layer
- Conservation of mass: No chemical transformation, deposition, or decay of pollutant during transport
- Flat terrain: Ground is assumed flat with complete reflection (no absorption)
- Gaussian distribution: Concentration profiles follow normal distributions in y and z directions
- Continuous emission: Source emits continuously from a single point at constant rate
Understanding the Terms
| Term | Physical Meaning | Effect on Concentration |
|---|---|---|
| Q / (π σy σz u) | Dilution by wind and turbulent spreading | Higher wind or more spreading lowers C |
| exp(-He² / 2σz²) | Vertical offset from source to receptor | Taller stacks reduce ground-level C |
| σy(x) | Lateral plume width, grows with distance | Wider spread dilutes concentration |
| σz(x) | Vertical plume depth, grows with distance | Deeper spread dilutes; but also brings plume to ground |
Maximum Ground-Level Concentration
The maximum ground-level concentration (GLC) occurs at the downwind distance where the vertical dispersion coefficient σz equals the effective stack height divided by the square root of 2:
This relationship shows that the maximum ground-level concentration is inversely proportional to the square of the effective stack height. Doubling the effective height reduces the maximum GLC by approximately 75%, making stack height one of the most effective controls for reducing ground-level impacts.
3. Atmospheric Stability (Pasquill-Gifford)
Atmospheric stability determines how rapidly a plume spreads as it travels downwind. The Pasquill-Gifford classification system divides atmospheric conditions into six stability classes, from very unstable (A) to very stable (F), based on wind speed, solar radiation, and cloud cover.
Stability Class Definitions
| Class | Description | Conditions | Dispersion Rate |
|---|---|---|---|
| A | Very Unstable | Strong sun, light wind (<2 m/s) | Very rapid |
| B | Moderately Unstable | Moderate sun, light-moderate wind | Rapid |
| C | Slightly Unstable | Slight sun or moderate wind | Moderate-fast |
| D | Neutral | Overcast, any wind speed | Moderate |
| E | Slightly Stable | Clear night, light-moderate wind | Slow |
| F | Very Stable | Clear night, light wind (<3 m/s) | Very slow |
Determining Stability Class
The Pasquill-Gifford stability class is determined by surface wind speed and the degree of insolation (daytime) or cloud cover (nighttime):
| Surface Wind Speed (m/s) | Daytime Insolation | Nighttime Cloud Cover | |||
|---|---|---|---|---|---|
| Strong | Moderate | Slight | ≥ 4/8 cloud | < 3/8 cloud | |
| < 2 | A | A-B | B | — | — |
| 2 – 3 | A-B | B | C | E | F |
| 3 – 5 | B | B-C | C | D | E |
| 5 – 6 | C | C-D | D | D | D |
| > 6 | C | D | D | D | D |
Dispersion Coefficients
The dispersion coefficients σy and σz are empirical functions of downwind distance and stability class, derived from tracer experiments. They represent the standard deviation of the concentration distribution in the lateral and vertical directions.
Typical Dispersion Coefficient Values
| Distance (m) | Class A (Very Unstable) | Class D (Neutral) | Class F (Very Stable) | |||
|---|---|---|---|---|---|---|
| σy (m) | σz (m) | σy (m) | σz (m) | σy (m) | σz (m) | |
| 100 | 22 | 15 | 7 | 4 | 4 | 1.5 |
| 500 | 92 | 140 | 32 | 14 | 16 | 6 |
| 1,000 | 170 | 520 | 60 | 24 | 29 | 10 |
| 5,000 | 680 | 5000+ | 260 | 67 | 115 | 28 |
| 10,000 | 1200 | 5000+ | 470 | 100 | 200 | 40 |
Values are approximate; actual coefficients vary by parameterization (Turner, ISC3, Briggs).
Effect of Stability on Plume Behavior
- Unstable (A, B): Strong vertical mixing creates a wide, short plume. Maximum concentrations occur close to the source and can be very high but dissipate rapidly. These conditions occur during sunny afternoons with light winds.
- Neutral (D): Moderate dispersion in all directions. This is the default assumption for overcast conditions and is often used as a reasonable average for long-term assessments.
- Stable (E, F): Suppressed vertical mixing creates a narrow, elevated plume that travels long distances before reaching the ground. Maximum concentrations are lower but occur at greater distances. These conditions occur during clear nights with light winds. Stable conditions are typically the worst case for elevated sources because the plume remains concentrated over longer distances.
4. Plume Rise (Briggs Equations)
Plume rise is the additional elevation gained by the exhaust gas after leaving the stack tip, caused by the gas being hotter and/or faster-moving than the surrounding atmosphere. The effective stack height equals the physical stack height plus the plume rise, and it is the effective height that determines ground-level concentrations.
Components of Plume Rise
Two mechanisms contribute to plume rise:
- Buoyancy rise: Hot exhaust gas is less dense than ambient air and rises due to thermal buoyancy. This is typically the dominant mechanism for industrial sources with high exhaust temperatures.
- Momentum rise: The vertical velocity of the gas exiting the stack carries the plume upward. This is significant for sources with high exit velocities but small temperature differences.
Diagram: Plume rise showing physical stack height Hs, plume rise delta-h, effective stack height He, and the transition from bent-over to level plume
Briggs Buoyancy Flux
Briggs Final Plume Rise Equations
The final plume rise depends on both the flux parameters and the atmospheric stability:
| Condition | Buoyancy Rise | Momentum Rise |
|---|---|---|
| Unstable/Neutral (A-D), Fb < 55 | Δh = 21.425 × Fb^(3/4) / u | Δh = 3 × d × Vs / u |
| Unstable/Neutral (A-D), Fb ≥ 55 | Δh = 38.71 × Fb^(3/5) / u | Δh = 3 × d × Vs / u |
| Stable (E, F) | Δh = 2.6 × (Fb / (u × s))^(1/3) | Δh = 1.5 × (Fm / (u × s^0.5))^(1/3) |
Typical Plume Rise Values
| Source Type | Stack Ht (ft) | Exit Temp (°F) | Exit Vel (ft/s) | Typical Plume Rise (ft) |
|---|---|---|---|---|
| Compressor engine exhaust | 30–60 | 700–1000 | 50–100 | 50–200 |
| Glycol reboiler stack | 20–40 | 300–400 | 20–40 | 15–60 |
| Line heater stack | 15–30 | 400–600 | 15–30 | 10–40 |
| Flare stack (tip velocity) | 100–300 | 1800–2500 | 60–400 | 100–500+ |
| Amine regenerator vent | 40–80 | 200–250 | 10–30 | 5–30 |
5. Stack Height Determination & GEP
Stack height is one of the most critical design parameters for controlling ground-level pollutant concentrations. The taller the stack, the greater the dilution before the plume reaches ground level. However, regulatory constraints prevent using excessively tall stacks as a substitute for emission controls.
Good Engineering Practice (GEP) Stack Height
EPA regulations at 40 CFR 51.100 define Good Engineering Practice stack height as the maximum creditable stack height for dispersion modeling purposes. Emissions credit cannot be taken for stack heights exceeding the GEP value.
Stack Height Selection Guidelines
| Factor | Consideration |
|---|---|
| Ambient standards | Stack must be tall enough that GLC does not exceed NAAQS/state standards at any receptor |
| Building wake | Stack should exceed GEP height (H + 1.5L) to avoid downwash |
| Regulatory cap | Credit limited to GEP height; excess height not credited in modeling |
| Structural/cost | Taller stacks cost more and require stronger foundations; balance against emission control alternatives |
| Exit velocity | Maintain Vs/u > 1.5 to avoid stack tip downwash; may require smaller diameter |
| FAA clearance | Stacks near airports may require FAA notification per 14 CFR 77 if over 200 ft AGL |
Regulatory Limitation: Per 40 CFR 51.100, a state cannot issue a permit that relies on stack heights exceeding GEP for demonstrating NAAQS compliance. If the GEP height is insufficient to achieve compliance, emission controls must be used to reduce Q rather than increasing stack height.
6. Building Downwash Effects
When a stack is located near a building, the aerodynamic wake created by the building can pull the plume down to ground level, dramatically increasing concentrations near the source. This phenomenon, called building downwash, is one of the most important considerations in stack design for midstream facilities where stacks are often located on or near compressor buildings, process buildings, or equipment skids.
Diagram: Building downwash showing recirculation cavity, wake zone, and plume behavior for stacks shorter and taller than GEP height
Downwash Mechanisms
- Cavity region: The immediate lee of the building creates a recirculation zone where concentrations can be very high. The cavity extends approximately 1.5L downwind of the building.
- Wake region: Beyond the cavity, enhanced turbulence from the building wake increases dispersion rates for 5–10 building heights downwind.
- Stack tip downwash: When exit velocity is less than 1.5 times the wind speed, the plume bends down behind the stack tip, reducing the effective emission height.
Stack Tip Downwash Correction
Huber-Snyder Building Downwash
When a stack is shorter than the GEP height, the Huber-Snyder method reduces the effective stack height to account for building wake effects. The reduction depends on the building dimensions relative to the stack height.
7. Terrain & Urban Effects
Terrain Classification
The terrain surrounding a facility significantly affects dispersion patterns. EPA categorizes terrain into three types for modeling purposes:
| Terrain Type | Description | Modeling Implications |
|---|---|---|
| Flat / Simple | No significant terrain features within 50 km; elevation changes < He | Standard Gaussian model applies directly |
| Rolling | Gentle hills, moderate relief; receptor elevations approach but do not exceed stack base | Enhanced vertical dispersion; 10–20% increase in sigma-z typical |
| Complex | Nearby terrain rises above effective stack height; valleys, ridgelines, or bluffs within 5–10 km | Requires specialized models (CTSCREEN, AERMOD with terrain). Gaussian plume may drastically underestimate concentrations at elevated receptors. |
Urban vs. Rural Dispersion
The urban heat island effect and increased surface roughness in urban areas enhance mechanical and thermal turbulence, causing greater plume dispersion. EPA accounts for this by shifting the stability classification toward neutral in urban areas:
| Rural Stability | Urban Equivalent | Rationale |
|---|---|---|
| A (Very Unstable) | B | Already well-mixed; urban roughness has smaller effect |
| B (Moderately Unstable) | C | Enhanced mixing reduces to slightly unstable |
| C (Slightly Unstable) | D | Urban mechanical turbulence shifts toward neutral |
| D (Neutral) | D | Already neutral; no adjustment |
| E (Slightly Stable) | D | Urban heat island prevents stable stratification |
| F (Very Stable) | D | Urban areas rarely achieve very stable conditions |
8. Regulatory Context
National Ambient Air Quality Standards (NAAQS)
Dispersion modeling is used to demonstrate that facility emissions will not cause or contribute to violations of the NAAQS established under 40 CFR 50:
| Pollutant | Averaging Period | Standard | Form |
|---|---|---|---|
| SO2 | 1-hour | 75 ppb (196 μg/m³) | 99th percentile of daily max, averaged over 3 years |
| NO2 | 1-hour | 100 ppb (188 μg/m³) | 98th percentile of daily max, averaged over 3 years |
| CO | 1-hour | 35 ppm (40,000 μg/m³) | Not to be exceeded more than once per year |
| CO | 8-hour | 9 ppm (10,000 μg/m³) | Not to be exceeded more than once per year |
| PM10 | 24-hour | 150 μg/m³ | Not to be exceeded more than once per year, averaged over 3 years |
| PM2.5 | 24-hour | 35 μg/m³ | 98th percentile, averaged over 3 years |
| PM2.5 | Annual | 9 μg/m³ | Annual mean, averaged over 3 years |
| Ozone | 8-hour | 70 ppb | Annual fourth-highest max, averaged over 3 years |
H2S Ambient Standards
There is no federal NAAQS for hydrogen sulfide (H2S), but many states have established ambient air quality standards or guidelines. Common state standards include:
| Jurisdiction | Standard | Averaging Period |
|---|---|---|
| Texas (TCEQ ESL) | 80 μg/m³ (56 ppb) | 1-hour |
| Louisiana | 150 μg/m³ | 1-hour |
| Wyoming | 70 μg/m³ | 30-minute |
| New Mexico | 10 ppb | 30-minute |
| North Dakota | 100 ppb | 1-hour |
| Alberta (Canada) | 14 μg/m³ (10 ppb) | 1-hour |
Key Regulatory Programs
| Program | Applicability | Modeling Requirement |
|---|---|---|
| PSD (Prevention of Significant Deterioration) | Major sources in attainment areas | Full NAAQS and increment analysis using AERMOD |
| NSR (New Source Review) | Major modifications in nonattainment areas | Ambient impact analysis required |
| Minor NSR | Minor sources / modifications | Screening analysis may suffice (SCREEN3) |
| 40 CFR 51.100 | All sources with stacks | GEP stack height requirements |
9. EPA Modeling Tiers
EPA's Guideline on Air Quality Models (40 CFR Part 51, Appendix W) establishes a tiered approach to dispersion modeling, from simple screening models to sophisticated refined models:
Tier 1: Screening Models
| Model | Application | Key Features |
|---|---|---|
| SCREEN3 | Single-source, flat terrain screening | Tests all stability/wind combinations; reports worst-case; no met data needed |
| AERSCREEN | AERMOD-based screening | AERMOD algorithms with default worst-case met; supersedes SCREEN3 |
| CTSCREEN | Complex terrain screening | 24-hour averaging; terrain data input |
Tier 2: Refined Models
| Model | Application | Key Features |
|---|---|---|
| AERMOD | Preferred EPA model for most applications | Planetary boundary layer theory; complex terrain; building downwash (BPIP-PRIME); 5 years hourly met data |
| CALPUFF | Long-range transport (>50 km) | Lagrangian puff model; time-varying met; coastal, complex terrain |
| OCD | Offshore/coastal sources | Overwater dispersion with shoreline fumigation |
When to Use Each Tier
- Screening (Tier 1): Initial feasibility studies, minor source permits, preliminary stack height design, emergency planning estimates. If the screening result shows compliance with a margin, no further analysis is needed.
- Refined (Tier 2): Required when screening analysis shows potential exceedances, for PSD/major NSR permits, when site-specific meteorology is available, or when terrain or building effects are complex.
References
- Pasquill, F. (1961). The estimation of the dispersion of windborne material. The Meteorological Magazine, 90, 33–49.
- Gifford, F.A. (1961). Use of routine meteorological observations for estimating atmospheric dispersion. Nuclear Safety, 2, 47–51.
- Briggs, G.A. (1969). Plume Rise. USAEC Critical Review Series, TID-25075.
- Briggs, G.A. (1971). Some recent analyses of plume rise observations. Proceedings, Second International Clean Air Congress.
- Briggs, G.A. (1975). Plume rise predictions. Lectures on Air Pollution and Environmental Impact Analysis, AMS, Boston.
- Turner, D.B. (1970). Workbook of Atmospheric Dispersion Estimates. EPA AP-26.
- EPA (1995). SCREEN3 Model User's Guide. EPA-454/B-95-004.
- EPA (2004). AERMOD: Description of Model Formulation. EPA-454/R-03-004.
- 40 CFR Part 50 — National Primary and Secondary Ambient Air Quality Standards.
- 40 CFR Part 51 — Requirements for Preparation, Adoption, and Submittal of Implementation Plans.
- 40 CFR 51.100 — Good Engineering Practice Stack Height.
- 40 CFR Part 51, Appendix W — Guideline on Air Quality Models.
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