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LNG Bunkering Risk Assessment Worksheet Templates

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LNG Bunkering Risks are a critical concern in the maritime industry, as the safe transfer of liquefied natural gas requires meticulous planning and execution. Effective risk assessment methodologies are essential to identify potential hazards and mitigate them before they escalate into serious incidents. By utilizing comprehensive worksheet templates, operators can systematically evaluate risks associated with LNG bunkering operations.

This proactive approach not only enhances safety but also ensures compliance with regulatory standards. Understanding and addressing these risks is vital for the sustainability and efficiency of marine fuel operations.

Introduction

Each LNG bunkering operation is unique and therefore, has a unique set of hazards and risks. This appendix introduces a risk assessment methodology, describes a process for performing a risk assessment, and provides example worksheet templates for a truck-to-vessel bunkering operation.

Risk Assessment Methodology

To characterize the risk of LNG Risk Assessment in the Liquefied Natural Gas Bunkering Operations, Hazard Identificationbunkering operations, risk assessment teams must tailor a sound risk assessment methodology that can successfully answer the following questions:

  • What can go wrong? Risk assessment methods are used to identify hazards that can create accidents. These can include equipment failures, human errors, and external events. Based on the quantity and types of hazards that may affect the bunkering option, analysts can gain a good understanding of the risk associated with the operation.
  • How likely is it? Likelihood is usually expressed as the probability or frequency of an accident occurring. If the likelihood is low enough, analysts may conclude that a possible accident scenario is not credible, not of concern, or of extremely low risk. But, the criteria for making such judgments often change with the type and severity of the consequence related to the possible accident.
  • What are the impacts? An accident can affect many areas of concern with different degrees of negative results. The type and severity of consequences related to an accident help an analyst understand and judge risk.

The following are key terms and definitions associated with the risk assessment process:

Hazards: Situations, conditions, characteristics, or properties that create the possibility of unwanted consequences.

Causes: Underlying reasons (e. g., equipment failure, human error) why the initial incident occurs and safeguards fail to interrupt the chain of events.

Safeguards: Planned protections that are intended to interrupt the progression of accident sequences at various points in accident chains of events. Safeguards can be applied to prevent the likelihood of occurrence or to minimize the consequences. These planned protections may be physical devices, human interventions, or administrative policies.

Likelihood: The likelihood of events is often expressed as a frequency, events per year. To assess the frequency of any event, analysts must consider (1) how often the hazard is present (e. g., how many times an operation is performed) and (2) the probability of experiencing the accident during any exposure to the hazard.

Table 1 is an example of likelihood categories.

Table 1. Likelihood Categories
CategoryCategory Descriptions
Almost Certain (E)Occurs 1 or more times per year
Likely (D)Occurs once every 1 to 10 years
Possible (C)Occurs once every 10 to 100 years
Unlikely (B)Occurs once every 100 to 1 000 years
Rare (A)Occurs once every 1 000 to 10 000 years

Consequences: Unwanted impacts that can negatively affect subjects of interest. These types of impacts can include: deaths/injuries to workers and the public, property damage, business interruption, environmental impacts, and impacts to company reputation. The severity of consequences can range from insignificant to catastrophic. Each owner/operator has unique considerations; therefore, impact and severity descriptions should be tailored to reflect organizational concerns. Table 2 provides an example of a consequence matrix containing representative impact and severity categories.

Table 2. Representative Consequence Categories
Severity CategoriesImpacts
Death & InjuryEconomicEnvironmentalReputation
Low (1)Low level short-term subjective inconvenience or symptoms. No measurable physical
effects. No medical
treatment.
No shutdown,
costs less than
$1 000 to repair.
No lasting effect. Low-level impacts on biological
or physical environment.
Limited damage to minimal area of low significance.
Public concern restricted to
local complaints. Ongoing
scrutiny/attention from regulator.
Minor (2)Objective but
reversible disability/
impairment and/or
medical treatment
injuries requiring
hospitalization.
No shutdown,
costs less than
$10 000 to repair.
Minor effects on biological or physical environment.
Minor short-term damage to small area of limited
significance.
Minor, adverse local public or media attention and complaints. Significant
hardship from regulator. Reputation is adversely affected with a small number of site-focused people.
Moderate (3)Moderate irreversible
disability or impairment (< 30 %)
to one or more persons.
Operations
shutdown, loss
of day rate for
1-7 1days and/or
repair costs of
up to $100 000.
Moderate effects on
biological or physical environment but not
affecting ecosystem
function. Moderate
short-medium term
widespread impacts (e. g., oil spill causing impacts on
shoreline).
Attention from media and/or
heightened concern by local community. Criticism by Non-
Governmental Organizations
(NGO). Significant difficulties in gaining approvals. Environmental credentials moderately affected
Major (4)Single fatality
and/or severe
irreversible disability
or impairment
(> 30 %) to one or
more persons.
Operations
shutdown, loss
of day rate for 7-28 days and/or repair
costs of up to $1 000,000.
Serious environmental
effects with some
impairment of ecosystem function (e. g., displacement
of species). Relatively widespread medium-long term impacts.
Significant adverse national media/public/NGO attention. May lose license to operate
or not gain approval.
Environment/management
credentials are significantly tarnished.
Critical (5)Short or long-term
health effects leading
to multiple fatalities,
or significant
irreversible health
effects to > 50 persons.
Operations
shutdown, loss
of day rate for
more than 28
days and/or repair costs more than
$1 000,000.
Very serious effects with impairment of ecosystem function. Long-term widespread effects on significant environment
(e. g., unique habitat,
National Park).
Serious public or media outcry
(international coverage).
Damaging NGO campaign. License to operate threatened. Reputation severely tarnished. Share price may be affected.

Risk: The risk of a hazard is based on the combination of the likelihood and consequence assessment, allowing risks of different hazards, operations, and potential accidents to be compared using a common measuring stick. Table 3 presents examples of risk levels assigned for each combination of likelihood and severity combination. Each owner/operator has unique considerations and risk tolerances, thus risk levels should be tailored to reflect those individual organizational risk tolerances.

Risk Levels
Table 3. Risk Levels

Risk Assessment Process

Accidents usually occur through a chain of events ending in one or more unwanted effects. This chain of events begins with hazards capable of causing consequences. If there are no hazards, there are no consequences. An equipment failure, human error, or external event is necessary for a hazard to cause consequences. Sometimes one or more equipment failures, human errors, or external events must take place after the initiating event for an accident to occur. An accident has at least one unwanted consequence with a measurable effect. This outcome is influenced throughout the chain of events by the presence of safeguards and their success or failure.

Read also: Guidance on HAZID and HAZOP for LNG bunkering operations

The risk assessment team should develop various accident chains for representative bunkering options by identifying potential hazards, causes, consequences, and safeguards by applying a sound methodology and structured assessment process (Figure).

Bunkering risks
Risk Assessment Processs

To do this, the team could employ the HazID methodology which leverages experts to brainstorm potential scenarios to facilitate in identification of health, safety, and environmental (HSE) hazards associated with various LNG Key Considerations for Successful Bunkering Facility Developmentbunkering options.

Key steps required to develop the risk profiles include:

  • Assemble an appropriate team of experts familiar with LNG loading/unloading operations and LNG bunkering.
  • Provide an overview of each bunkering option, including major phases of the operations (e. g., connect, transfer, disconnect, lift) and types of vessels involved.
  • Brainstorm hazards that could potentially result in unwanted consequences.
  • Identify potential causes of the hazard.
  • Identify safeguards potentially in place to prevent the likelihood of occurrence (prevention) or minimize the consequences (mitigation).
  • Describe the consequences and, if the hazard could result in a release of LNG, score the risk of the hazard as a function of likelihood and consequence considering all impact types: deaths/injuries, economic impacts, environmental impacts, and impacts to company reputation.
  • If applicable, document the linkage between hazards that could be causes of other hazards.
  • Record the team’s discussions on HazID worksheets.

LNG bunkering within North America is early in its development and there is relatively limited experience internationally. Therefore, at this time, there is a lack of historical accident data on which to base the risk assessment. To develop the risk profile, the team should consider hazards, causes, and consequences for historical accidents of analogous operations, including LNG import/export, traditional bunkering, and hazardous material transfers.

Table 4 provides an example worksheet template for a truck-to-vessel bunkering operation.

Table 4. Template Worksheet for Truck to Vessel Hazard Assessment
No. 1Truck to Vessel
ItemHazardTypical CausesTypical ConsequencesImpactSLRisk LevelRepresentative Safeguards
1.1What if there is
an LNG leak from
pump/piping/
hoses during
transfer?
Corrosion/erosion
External impact
Fatigue failure
Gasket, packing failure
Hose failure or disconnection
Improper hose connection
Improper maintenance
Material defect (e. g., weld)
Piping not properly cooled
down prior to transfer.
Seal failure.
Use of inappropriate piping/
hoses (e. g., not LNG rated)
Valve leaking or misaligned to
the atmosphere
VibrationExcessive movement of the
loading arm (linked from 1.5)
Supply truck drives/rolls away
with hoses still connected
(linked from 1.10)
Another vessel collides with
the receiving vessel (linked
from 1.11)Cargo dropped onto tank or
loading lines (linked from 1.13)
Fire aboard the receiving
vessel (linked from 1.14)Extreme sea state (linked from
1.17)
Earthquake (linked from 1.18)

Small release of LNGEnvironmentalBunkering procedures
Communication between parties involved in bunkering (e. g., person in charge)

Controls and/or prohibitions of simultaneous
passenger and bunkering operations
Designed breakaway coupling protects other
equipmentDrip tray
Equipment inspection/testing prior to bunkering
ESD system
ESD system tests
Flammable material detectors
Maintenance procedures
Personal protective equipment
Pressure testing
Supervision during transfer operations
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Periodic certification of hoses
Vessel emergency response plans
Local emergency response plans

Small release of LNG, resulting
in brittle fracture of ship deck;
fire damage to ship/supply tank/
surrounding equipment potentially
affecting a small area
Economic
Small release of LNG, resulting in
fire/explosion/cryogenic hazards to
personnel in the immediate area
Death & Injury
1.2What if there is
an LNG leak from
the supply truck?
Corrosion/erosion
External impact
Gasket/packing failure
Improper maintenance
Material defect
Valve leaking or misaligned to
the atmosphere
Vehicle collides with the
supply truck (linked from 1.12)
Cargo dropped onto tank or
loading lines (linked from 1.13)
Earthquake (linked from 1.18

Small release of LNGEnvironmentalBunkering procedures
Controls and/or prohibitions of simultaneous
passenger and bunkering operations
Equipment inspection/testing prior to bunkering
ESD system
ESD system tests
Bunkering of Liquefied Natural Gas-fueled Marine Vessels in North America
No. 1 Truck to Vessel
Item Hazard Typical Causes Typical Consequences Impact S L Risk Level Representative Safeguards
Vehicle collides with the
supply truck (linked from 1.12)
Cargo dropped onto tank or
loading lines (linked from 1.13)
Earthquake (linked from 1.18)
Flammable material detectors
Maintenance procedures
Personal protective equipment
Supervision during transfer operations
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Periodic certification of hoses
Vessel emergency response plans
Local emergency response plans

Small release of LNG, resulting in
fire damage to ship/supply tank/
surrounding equipment potentially
affecting a small area
Economic
Small release of LNG, resulting in
fire/explosion/cryogenic hazards to
personnel in the immediate area
Death & Injury
1.3What if there is
a disconnect of
piping/hoses
during transfer
(prior to stopping
flow)?
Improper connection
Excessive movement of the loading arm (linked from 1.5)Supply truck drives/rolls away with hoses still connected
(linked from 1.10)
Another vessel collides with the receiving vessel (linked
from 1.11)
Cargo is dropped onto loading lines (linked from 1.13)
Extreme sea state (linked from 1.17)

Very small release of LNGEnvironmentalBunkering procedures
Communication between parties involved in bunkering (e. g., person in charge)
Controls and/or prohibitions of simultaneous
passenger and bunkering operations
Designed breakaway coupling protects other
equipment
Drip tray
Equipment inspection/testing prior to bunkering
ESD system
ESD system tests
Flammable material detectors
Maintenance procedures
Personal protective equipment
Supervision during transfer operations
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Vessel emergency response plans
Local emergency response plans
Very small release of LNG, resulting in cryogenic hazards to personnel in the immediate areaDeath & Injury
Very small release of LNG; no
economic consequence
1.4What if the ESD
system fails to
stop LNG flow
when leak or
inadvertent
disconnect
occurs?
ESD instrumentation failure
Icing on piping and/or valves
interferes with ESD function
No ESD system on supply
truck
Operator error/interference
with ESD function
Programming errors (e. g.improper logic)
Use of nonstandard equipment
Large release of LNGEnvironmentalAbility to manually initiate ESD system
Bunkering equipment configuration control
Bunkering procedures
ESD system checkout and periodic testing
Personal protective equipment
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Vessel emergency response plans
Local emergency response plans
Large release of LNG, resulting
in brittle fracture of ship deck;
fire damage to ship/supply tank/
surrounding equipment potentially
affecting a large area
personnel in the surrounding area
Economic
Serious media attention and public
outcry
Reputation
1.5What if there
is excessive
movement of
the hose/loading
arm?
External impact
Improper maintenance
Loading arm control system
failure
Operator error in placing and
adjusting loading arm
Structural failure
Extreme wind (linked from 1.16)
Earthquake (linked from 1.18)
LNG leak from pump/piping/hoses
during transfer (linked to 1.1)
Bunkering procedures
ESD system
Loading arm design standards and inspections
Maintenance procedures
Disconnect of piping/hoses during
transfer (prior to stopping flow)
(linked to 1.3)
1.6What if the tank
is overfilled?
Level controller and operator
fail to stop flow when tank is ful
Small to medium release of LNGEnvironmentalBunkering procedures
High level alarm
Independent level inputs to ESD system
Personal protective equipment
Tank instrumentation
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Vessel emergency response plans
Local emergency response plans
Small to medium release of LNG,
resulting in brittle fracture of ship
deck/fire damage to ship/supply
tank/surrounding equipment
potentially affecting a small area
Economic
Small to medium release of LNG,
resulting in fire/explosion/ cryogenic hazards to personnel in a small area
Death & Injury
1.7What if
the tank is
overpressured?
Continued transfer to liquid-
full tank and relief valve fails to open
Fire aboard the receiving
vessel (linked from 1.14)
Large release of LNGEnvironmentalBunkering procedures, including emergency
operations
ESD system shut off on high level
Personal protective equipment
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Vessel emergency response plans
Local emergency response plans
Large release of LNG, resulting
in brittle fracture of ship deck/
fire damage to ship/supply tank/
surrounding equipment potentially
affecting a large area
Economic
Large release of LNG, resulting in
fire/explosion/cryogenic hazards to
personnel in the surrounding area
Death & Injury
Serious media attention and public
outcry
Reputation
1.8What if the
transfer lines
are not de-
inventoried
and/or purged
properly?
Operator errorSmall release of LNGEnvironmentalBunkering procedure, including: de-inventorying,
purging, inerting, and disconnection steps
Operator training
Small release of LNG, resulting
in brittle fracture of ship deck;
fire damage to ship/supply tank/
surrounding equipment potentially
affecting a small area
Economic
Small release of LNG, resulting in
fire/explosion/cryogenic hazards to
personnel in the immediate area
Death & InjuryPersonal protective equipment
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Vessel emergency response plans
Local emergency response plans
1.9What if LNG
(cryogenic liquid)
is blocked in
between two
valves?
Improper purgingDamage to valve/pipingEconomicBunkering procedure, including: de-inventorying,
purging, inerting, and disconnection steps
Personal protective equipment
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Very small release of LNGEnvironmental
Very small release of LNG, resulting in cryogenic hazards to personnel in the immediate areaDeath & Injury
1.10What if the
supply truck
drives/rolls away
with hoses still
connected?
Failure to secure truck (brakes,
wheel chocks)
Truck driver error
Vehicle collides with the
supply truck (linked from 1.12)
LNG leak from pump/piping/hoses
during transfer (linked to 1.1)
Bunkering procedures, including steps to secure
supply truck
Driver training
Limit traffic in bunkering area
Disconnect of piping/hoses during
transfer (prior to stopping flow)
(linked to 1.3)
1.11What if another
vessel collides
with the receiving vessel?
Error in ship navigation by passing ship
Poor visibility
Steering or propulsion failure in passing ship
LNG leak from pump/piping/hoses
during transfer (linked to 1.1)
Mariner training and credentials
Piloted operations, where employed
USCG safety zones and regulated navigational areas
Disconnect of piping/hoses during
transfer (prior to stopping flow)
(linked to 1.3)
1.12What if a vehicle
collides with the
supply truck?
Driver errorLNG leak from the supply truck
(linked to 1.2)
Bunkering procedures
Driver training
Limited traffic in bunkering area
Vehicle guards around fixed storage tank
Truck drives/rolls away with hoses
still connected (linked to 1.10)
1.13What if cargo is
dropped onto
supply truck or
loading lines?
Crane operator error
Crane structural failure
Improper maintenance
Use of equipment with
insufficient lifting capacity
Extreme wind (linked from 1.16)
Earthquake (linked from 1.18)
LNG leak from pump/piping/hoses
during transfer (linked to 1.1
Bunkering procedures
Controls and/or prohibitions of simultaneous cargo and bunkering operations
Crane design standards and inspections
Crane operator training and certification
Maintenance procedures
LNG leak from the supply truck
(linked to 1.2)
Disconnect of piping/hoses during
transfer (prior to stopping flow)
(linked to 1.3)
1.14What if there is
a fire aboard the
receiving vessel?
Galley, engine room,
passenger compartment fire
LNG leak from pump/piping/hoses
during transfer (linked to 1.1)
Bunkering procedures, including emergency
operations
ESD system
Firefighting system
Shipboard emergency response procedures
Tank is overpressured (linked to 1.7)
1.15What if there is
an external fire
near the supply
truck?
Onshore/dock fire
Transportation equipment fire
Large release of LNGEnvironmentalBunkering procedures, including emergency operations
ESD system
Facility emergency response procedures
Facility firefighting system
Personal protective equipment
Appropriate electrical classification in bunkering area
where accidental releases could occur to limit ignition
sources
Vessel emergency response plans
Local emergency response plans
Large release of LNG, resulting
in fire/explosion damage to ship/
supply tank/surrounding equipment potentially affecting a large area
Economic
Large release of LNG, resulting in
fire/explosion/BLEVE/cryogenic
hazards to personnel in the
surrounding area
Death & Injury
Serious media attention and public
outcry
Reputation
1.16What if there
is extreme
wind during
the bunkering
operation?
WeatherExcessive movement of the loading arm (linked to 1.5)Bunkering procedures, including weather limits
Cargo is dropped onto tank or
loading lines (linked to 1.13)
1.17What if there is
an extreme sea
state during
the bunkering
operation?
WeatherLNG leak from pump/piping/hoses
during transfer (linked to 1.1)
Bunkering procedures, including weather limits
Disconnect of piping/hoses during
transfer (prior to stopping flow)
(linked to 1.3)
1.18What if there is
an earthquake
during the
bunkering
operation?
EarthquakeLNG leak from pump/piping/hoses
during transfer (linked to 1.1)
Seismic qualifications of cranes
Seismic qualifications of fixed onshore tanks
LNG leak from the supply truck
(linked to 1.2)
Excessive movement of the loading arm (linked to 1.5)
Cargo dropped onto tank or loading lines (linked to 1.13
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Author
Author photo - Olga Nesvetailova
Freelancer

Literature
  1. Study on the completion of an EU framework on LNG-fuelled ships and its relevant fuel provision infrastructure, LOT 1 Position paper: Towards harmonized EU LNG bunkering guidelines, DNV-GL, 2016.
  2. Study on the completion of an EU framework on LNG-fuelled ships and its relevant fuel provision infrastructure, LOT 1 Final Report, DNV-GL, 2016.
  3. LNG Bunkering Guidelines IACS Recommendation n. 142, on LNG Bunkering, IACS, 2016.
  4. ISO/TS 18683:2015. (15-Jan. 2015). Guidelines for systems and installations for supply of LNG as fuel to ships. Technical Specification.
  5. Society for Gas as a Marine Fuel (SGMF). (2015). Gas as a marine fuel, safety guidelines, Bunkering. Version 1.0, February 2015.
  6. ISO 20519:2017. Ships and marine technology – Specification for bunkering of gas fuelled ships. (International Standard).
  7. IEC 60079-10-1. (2015). Explosive atmospheres – Part 10-1: Classification of areas – Explosive gas atmospheres.
  8. Directive 1999/92/EC – ATEX of the European Parliament and of the Council of 16 December 1999 on minimum requirements for improving the safety and health protection of workers potentially at risk from explosive atmospheres (15th individual Directive within the meaning of Article 16(1) of Directive 89/391/EEC).
  9. API RP-500. 1997. Recommended practice for classification of locations for electrical installations at petroleum facilities classified as CIass 1, Division 1 and Division 2. Washington. D.C: API.
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  11. NFPA 497. 2012, Recommended practice for the classification of flammable liquids, gases or vapours and of hazardous (classified) locations for electrical installations in chemical process areas. Quincy, MA: NFPA.
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  14. USCG CG-OES Policy Letter 02-14 – Guidance Related To Vessels And Waterfront Facilities Conducting Liquefied Natural Gas (LNG) Marine Fuel Transfer (Bunkering) Operations.
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  16. ADR – European agreement concerning the International Carriage of Dangerous Goods by Road (Update version ADR January 2017).
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  23. LNG Access Code for Truck Loading for The Zeebrugge LNG Terminal – Based on version approved by the CREG on September 19th 2013 – Applicable as of January 1st 2014 – FLUXYS.
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  26. Verhoeven P (2010) A review of port authority functions: towards a renaissance? Marit Policy Manag 37:247-270.
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  28. COM(2003) 515 final – Communication from The Commission concerning the non-binding guide of good practice for implementing Directive 1999/92/EC of the European Parliament and of the Council on minimum requirements for improving the safety and health protection of workers potentially at risk from explosive atmospheres, Brussels, 25.8.2003.
  29. Davies, P. (2016) – Bunkering LNG: Setting the Safety Zone, 7th Motorship Gas Fuelled Ships Conference, November 2016.
  30. International Association of Oil & Gas Producers. (1-Mar 2010). Risk Assessment Data Directory – Process Release Frequencies. Report No. 434 – 1, 1 March 2010). Pertinent data from this report is summarised in: Davies & Fort, (Sept 2012), LNG as Marine Fuel – Likelihood of LNG Releases, Journal of Marine Engineering and Technology.
  31. PGS2 – TNO Yellow Book – Methods for the calculation of physical effects, due to releases of hazardous materials (liquids and gases) – CPR 14E (3rd Edition, 2005) – TNO – The Netherlands Organization of Applied Scientific Research.
  32. OECD Guiding Principles for Chemical Accident Prevention, Preparedness and Response, Guidance for Industry (including Management and Labour), Public Authorities, Communities, and other Stakeholders – 2nd Edition (2003) – OECD Environment, Health and Safety Publications.
  33. DNVGL-RP-G105 Edition October 2015 – Development and operation of liquefied natural gas bunkering facilities, Recommended Practice, DNV GL, 2015.
  34. USCG CG-OES Policy Letter No. 01-17 – Guidance for Evaluating Simultaneous Operations (SIMOPS) during Liquefied Natural Gas (LNG) Fuel Transfer Operations.
  35. LGC NCOE Field Notice 01-2017 – 14-Aug-17 – Recommended Process For Analysing Risk Of Simultaneous Operations (SIMOPS) During Liquefied Natural Gas (LNG) Bunkering.
  36. An Overview of Leading Software Tools for QRA, American Society of Safety Engineers – Middle East Chapter (161), 7th Professional Development Conference & Exhibition, March 18-22, 2005.
  37. Walter Chukwunonso Ikealumba and Hongwei Wu (2016) Some Recent Advances in Liquefied Natural Gas (LNG) Production, Spill, Dispersion, and Safety School of Chemical and Petroleum Engineering, Curtin University.

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