Environmental & Safety Engineering

Atmospheric Dispersion Modeling for Midstream Facilities

Understand Gaussian plume dispersion theory, Pasquill-Gifford stability classifications, Briggs plume rise equations, and EPA regulatory frameworks for stack height design and air quality compliance at pipeline and gas processing facilities.

Primary Model

Gaussian Plume

EPA standard screening method

Stability Classes

A through F

Pasquill-Gifford (1961)

Key Regulation

40 CFR 51

GEP stack height & modeling

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
Screening vs. Refined Modeling: Screening models (SCREEN3) use simplified, conservative assumptions and are appropriate for initial assessments. If a screening analysis shows potential exceedances, refined models (AERMOD, CALPUFF) with actual meteorological data are required for permit applications.

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:

Full Gaussian Plume Equation: C(x,y,z) = Q / (2π σy σz u) × exp(-y² / 2σy²) × { exp(-(z-He)² / 2σz²) + exp(-(z+He)² / 2σz²) } Ground-Level Centerline (y=0, z=0): C(x,0,0) = Q / (π σy σz u) × exp(-He² / 2σz²) Where: C = concentration (μg/m³) Q = emission rate (g/s) σy = lateral dispersion coefficient (m) σz = vertical dispersion coefficient (m) u = wind speed at effective stack height (m/s) He = effective stack height = Hs + Δh (m) Hs = physical stack height (m) Δh = plume rise (m) x = downwind distance (m) y = crosswind distance (m) z = vertical height above ground (m)

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:

Condition for Maximum GLC: σz = He / √2 At this distance, the maximum GLC is: C_max = 2Q / (π e u He²) × (He / σy_max) Simplified approximation: C_max ≈ 0.117 × Q / (u × σy × He) Where: e = 2.71828 (Euler's number) σy_max = sigma-y at the distance where σz = He/√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
< 2AA-BB
2 – 3A-BBCEF
3 – 5BB-CCDE
5 – 6CC-DDDD
> 6CDDDD

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.

Pasquill-Gifford Dispersion Coefficients: σy = a × x^b σz = c × x^d Where: x = downwind distance (km for ISC3 parameterization) a, b, c, d = empirical coefficients (stability-dependent) General Behavior: - σy and σz increase with distance (plume grows) - Unstable (A, B): rapid growth, wide plumes - Stable (E, F): slow growth, narrow plumes - σz is capped at mixing height (~1000-2000 m)

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)
10022157441.5
500921403214166
1,00017052060242910
5,0006805000+2606711528
10,00012005000+47010020040

Values are approximate; actual coefficients vary by parameterization (Turner, ISC3, Briggs).

Worst-Case Stability: For screening analyses, stability class F (very stable) with low wind speed (1–2 m/s) typically produces the highest ground-level concentrations at rural sites. However, class A or B may produce higher concentrations very close to the stack. EPA SCREEN3 tests all classes and reports the maximum.

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

Buoyancy Flux Parameter (Fb): Fb = g × Vs × d² × (Ts - Ta) / (4 × Ts) Where: g = gravitational acceleration (9.81 m/s²) Vs = stack exit velocity (m/s) d = stack inside diameter (m) Ts = stack gas temperature (K) Ta = ambient temperature (K) Fb = buoyancy flux parameter (m&sup4;/s³) Momentum Flux Parameter (Fm): Fm = Vs² × d² × Ta / (4 × Ts) Units: m&sup4;/s²

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)
Stability Parameter (s): s = (g / Ta) × (dθ/dz) Typical potential temperature gradients: Class E: dθ/dz = 0.020 K/m Class F: dθ/dz = 0.035 K/m Effective Stack Height: He = Hs + max(Δh_buoyancy, Δh_momentum) The larger of buoyancy and momentum rise is used.

Typical Plume Rise Values

Source Type Stack Ht (ft) Exit Temp (°F) Exit Vel (ft/s) Typical Plume Rise (ft)
Compressor engine exhaust30–60700–100050–10050–200
Glycol reboiler stack20–40300–40020–4015–60
Line heater stack15–30400–60015–3010–40
Flare stack (tip velocity)100–3001800–250060–400100–500+
Amine regenerator vent40–80200–25010–305–30
Design Implication: Plume rise can increase the effective stack height by 50% to 200% or more for hot, buoyant sources. This means a 100-ft compressor exhaust stack with 700°F exit temperature may have an effective height of 200–300 ft, significantly reducing ground-level concentrations. Always account for plume rise when sizing stacks.

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.

GEP Stack Height (40 CFR 51.100): GEP = H + 1.5L Where: H = height of nearby structure(s) L = lesser dimension of: - height of the structure, or - projected width of the structure Default GEP Formula (no structures): GEP = 65 meters (213 feet) If stack < GEP height: Building downwash corrections must be applied. If stack > GEP height: Only the GEP height is credited for modeling.

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

Stack Tip Downwash (Briggs): When Vs < 1.5 × u: Hs_adj = Hs + 2d(Vs/u - 1.5) Where: Vs = stack exit velocity (m/s) u = wind speed at stack height (m/s) d = stack inside diameter (m) Prevention: Maintain Vs / u ≥ 1.5 at all times. For a design wind speed of 5 m/s: Vs ≥ 7.5 m/s (25 ft/s)

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.

Practical Rule: For midstream compressor stations, the stack should be at least 2.5 times the height of the nearest building or major equipment structure to avoid significant downwash effects. If this is not feasible, use the building downwash correction in the dispersion model and verify that ground-level concentrations remain acceptable.

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)BAlready well-mixed; urban roughness has smaller effect
B (Moderately Unstable)CEnhanced mixing reduces to slightly unstable
C (Slightly Unstable)DUrban mechanical turbulence shifts toward neutral
D (Neutral)DAlready neutral; no adjustment
E (Slightly Stable)DUrban heat island prevents stable stratification
F (Very Stable)DUrban areas rarely achieve very stable conditions
For Midstream Facilities: Most pipeline compressor stations, gas plants, and gathering facilities are in rural settings. Use rural dispersion coefficients unless the facility is within an urbanized area (population > 50,000 within 3 km). Urban areas rarely experience the very stable conditions (E, F) that produce worst-case ground-level concentrations from elevated sources.

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
SO21-hour75 ppb (196 μg/m³)99th percentile of daily max, averaged over 3 years
NO21-hour100 ppb (188 μg/m³)98th percentile of daily max, averaged over 3 years
CO1-hour35 ppm (40,000 μg/m³)Not to be exceeded more than once per year
CO8-hour9 ppm (10,000 μg/m³)Not to be exceeded more than once per year
PM1024-hour150 μg/m³Not to be exceeded more than once per year, averaged over 3 years
PM2.524-hour35 μg/m³98th percentile, averaged over 3 years
PM2.5Annual9 μg/m³Annual mean, averaged over 3 years
Ozone8-hour70 ppbAnnual 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
Louisiana150 μg/m³1-hour
Wyoming70 μg/m³30-minute
New Mexico10 ppb30-minute
North Dakota100 ppb1-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.
This Calculator's Role: The MidstreamCalculator stack dispersion tool is a Tier-1 screening-level model equivalent to SCREEN3. It uses the Gaussian plume equation with Pasquill-Gifford coefficients and Briggs plume rise. It tests all stability/distance combinations to find the maximum ground-level concentration. For permit applications, results should be confirmed with AERMOD or another EPA-approved refined model.

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.