TRAINING ONLINE GAS DISPERSION ANALYSIS
TRAINING WEBINAR ANALISA GAS DISPERSION
TRAINING PENGENALAN GAS DISPERSION ANALYSIS UNTUK PRAKERJA
GAS DISPERSION ANALYSIS TRAINING INTRODUCTION pelatihan analisa gas dispersion online
Oil and gas plants inherently emphasize the importance of planning for
emergency and designing plant to minimize the occurrence of toxic
release, or uncontrolled flammable gas into the surrounding and the
environments. Hence, it is of critically important to understand the
dispersion characteristics and to reduce the impact that may generate
during plant operation. Accidents results from loss of containment of
the gas from the process through various mechanism including leak,
rupture, runway reactions, etc. The rate of discharge, quantity
released, and dangerous concentrations levels are among important
factors to determine. Therefore, to be able to model gas dispersion as
a function of time and space, engineers must be able to : i) Identify
the release points, ii) develop a source model to describe how
materials are released and the rate of release, and iii) estimate the
downwind concentration of toxic or flammable material using
dispersions model. In this training, relevant DOW’s Chemical Exposure
Index, ERPGs, OSHA (CFR 1910,119), NFPA, and NRC references will be
consulted.
GAS DISPERSION ANALYSIS TRAINING OUTLINE pelatihan pengenalan gas dispersion analysis online
1. Introduction of Source Model
2. Flow of Vapor and Gas through Holes and Pipes
3. Adiabatic Flows and Isothermal Flows
4. Parameters Affecting Gas Dispersion
5. Neutrality Buoyant Dispersions Model (Plume and Puff Models with
respect to various wind, and release point location scenarios)
6. Dense Gas Dispersion
7. Toxic Effect Criteria
8. Effect of Release Momentum and Buoyancy
9. Gas Release Mitigation
GAS DISPERSION ANALYSIS TRAINING BENEFIT pelatihan gas dispersion online
In addition to QRA result, the operator will know the areas downwind
posses the high probability of the gas dispersion, the quantity and
the impact generates. Hence, the measures and precaution can properly
be anticipated. This highly quantitative analysis will be useful for
both during design stage as and operation stage of the plant.
WHO SHOULD ATTEND THIS TRAINING?
Plant and Pipeline Operators, Supervisors, Engineers and Manager.
Trainer : Bapak Arief Adinoto, S.E dan Tim
Jadwal pelatihan :
Batch 1 : 20 – 21 Januari 2026
Batch 2 : 10 – 11 Februari 2026
Batch 3 : 3 – 4 Maret 2026
Batch 4 : 14 – 15 April 2026
batch 5 : 19 – 20 Mei 2026
batch 6 : 24 – 25 Juni 2026
batch 7 : 8 – 9 Juli 2026
batch 8 : 19 – 20 Agustus 2026
batch 9 : 16 – 17 September 2026
batch 10 : 7 – 8 Oktober 2026
batch 11 : 18 – 19 November 2026
batch 12 : 9 – 10 Desember 2026
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