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 22 nd 2017

Transcript of LNG Topic Duisburg - Germany...LNG aspects in the Netherlands 8 Calculating safety distances by o...

Page 1: LNG Topic Duisburg - Germany...LNG aspects in the Netherlands 8 Calculating safety distances by o Programs like Phast DNV, Effects, Safeti to give an indication of the effects on thermic

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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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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12 juni 2008 Titel van de presentatie 30

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