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Toxic Gas Dispersion (Pasquill-Gifford)

Process safety Β· Gaussian plume w/ Briggs Οƒ Β· ALOHA-class

Continuous Gaussian-Plume Dispersion
Ground-level centreline concentration from a steady point release using the Gaussian plume with Briggs (1973) urban/rural dispersion coefficients, compared to user ERPG/AEGL endpoints.
⚠ Safety-critical β€” screening, neutral-buoyancy only. Passive plume, flat terrain, steady wind β‰₯ 0.5 m/s. INVALID for dense gases (chlorine, LPG vapour), complex terrain, building wakes, or calm winds β€” use a dense-gas model (DEGADIS/SLAB/Phast). Concentration vs endpoints (not dose/probit). Not for safety case submission or regulatory filing without SME review.

Release & Met

g/s
m/s

Geometry & Substance

m
m
Β°C

Toxic Endpoints (ppm, optional)

Engineering Basis

  • C = Q/(π·uΒ·ΟƒyΒ·Οƒz)Β·exp(βˆ’HΒ²/2ΟƒzΒ²) β€” ground-level centreline, continuous source.
  • Briggs (1973) open-country & urban Οƒy, Οƒz vs distance and Pasquill class A–F.
  • ppm = C[mg/mΒ³]Β·Vm/MW, Vm = 22.414Β·(T/273.15) L/mol.
  • Compare to ERPG-1/2/3 or AEGL endpoints (user input).
  • Standards: Briggs 1973 (Hanna/Briggs/Hosker 1982), Pasquill-Gifford, EPA ALOHA.