LNG Topic Duisburg - Germany...LNG aspects in the Netherlands 8 Calculating safety distances by o...
Transcript of LNG Topic Duisburg - Germany...LNG aspects in the Netherlands 8 Calculating safety distances by o...
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LNG aspects in the Netherlands 2
LNG Topic Duisburg - Germany Dutch approach: LNG Emergency Response development
Brian Paul Mo-Ajok, MSc.
Program manager national expert centre
February 22nd 2017
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Topics • Short introduction
• LNG
– Methods to assess
– Small scale
– Large scale
• Main concern
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Topics • Introduction
• LNG
– Methods to assess
– Small scale
– Large scale
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Reveal all mysteries
Sharing knowledge
Research
Scenario training
Evaluation incidents & near misses
Education
Private & public parties, scientists, educational institutes & consultants
Guidelines Detection Gap analyses
Awareness
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Topics • Introduction
• LNG
– Methods to assess
– Small scale
– Large scale
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Calculating safety distances by o Programs like Phast DNV, Effects, Safeti to give an indication of the effects on
thermic and concentration (Quick & dirty methods) o More specific with Computational Fluid Dynamics o Literature study o Depends on:
A. Source type (liquid, gas, vapour, composition) B. Atmospheric conditions (wind, temperature, humidity, turbulence) C. Ground effects (surface, heat flux, obstacle)
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Topics • Introduction
• LNG
– Methods to assess
– Small scale
– Large scale
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Methane LFL 5% UFL 15% LFL=lower flammable limit
UFL=upper flammable limit
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Evaporating rate in water 15 m3/min/m2
Evaporating rate on land (depends on type of soil) 3 m3/min/m2 In steady state 0,3 m3/min/m2
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Possible impact of an accident with LNG? o Type release -> Atm. Pressure (instantaneous vs continuous) pool fire, vapour
cloud explosion, flash fire, cryogenic effects o -> 4 Bar(g) (instantaneous vs continuous) BLEVE, fire ball, flash fire, jet fool
and the rest as mentioned above Prohibited areas for the storage and bunkering of LNG, near schools and
hospitals and other (partly) dependent people
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Safety standards for staff/crews (distances) Distances o Loss of control in gas (LEL Distance: 250*D) o Loss of control in liquid (LEL Distance: 500*D) o Flare Distance in liquid: 250*D o Flare Distance in gas: 500*D o Evacuation and preventing ignition sources 2*Flare Distance or 2*LEL Distance
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Small scale
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More information via:
National Expert Centre for Industrial Safety Program manager Impulse for Landscape Safety B.P. Mo-Ajok MSc. T: +31(0)63080 6365 [email protected] | www.BrandweerBRZO.nl P.O. Box 9154, 3007 AD Rotterdam, The Netherlands Langs de Baan 110, 3191 TP Rotterdam, The Netherlands
22 LNG aspects in the Netherlands
• Introduction
• LNG
– Methods to assess
– Small scale
– Large scale
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Topics • Introduction
• LNG
– Methods to assess
– Small scale
– Large scale
• Main concern: Salvage & Maintenance
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Disaster Management
Emergency response - fire
Emergency response - rescue
Disruption business as usual
Mutual Aid – LNG (e.g. TUI)
Steel structures failing
Major pool or gas release
Roll over truck
Transfer content damage teuck
Flare
Leakage in gas fase
Maintenance pipework valves
Prevent BOG
Disturbance/error in LNG instruments Operator LNG system
LNG intervention
Fire Medical Police
Ministerium
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So….
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Shared responsibilities
Sustain business/ fluent infrastructure
Smooth & safe
Emergency response
Good governance Protecting
People & Planet
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National Expert Centre for Industrial Safety (Seveso) Emergency response, disaster management, land use planning [email protected] +31(0)6-30806365 +31(0)888 – 779 556