The vast and complex world of maritime operations, encompassing everything from international shipping to offshore energy exploration, relies on a bedrock of stringent regulations and best practices. These maritime standards are not merely guidelines; they are critical frameworks designed to ensure safety at sea, protect the marine environment, and facilitate efficient global trade. As technology advances and environmental concerns grow, the evolution and adherence to these standards become increasingly vital, shaping the future of an industry that underpins the global economy.
This article will delve into the multifaceted nature of maritime standards, exploring their significance, the key organizations responsible for their development, and the ongoing challenges and innovations in their implementation.
Standards
Standards are fundamental to make the bridge between high level instruments, such as the ones presented in the previous section, and the operational, or technical, implementation of their provisions. The present section makes only reference to international standards developed and published by international standardization bodies (ISO, CEN and IEC). Other relevant references, supporting standardization in best practices, in particular the ones developed and commonly accepted by industry associations are included in Section “Other References”.
The importance of international standards in Functional and General Requirements for LNG Bunkering OperationLNG bunkering, working together with global reaching regulations, is directly related to the promotion of safety and confidence in the development of LNG as fuel for shipping. By setting out requirements for specific items, material, components, systems or equipment, or describing in detail a particular method or procedure, international standards facilitate international trade by ensuring compatibility and interoperability of components, products and services.
They bring benefits to operators and authorities in terms of reducing costs, enhancing performance and improving safety. Standards are developed and defined through a process of sharing knowledge and building consensus among technical experts nominated by interested parties and other stakeholders – including businesses, consumers and environmental groups, among others.
The formal definition of a standard is a “document, established by consensus and approved by a recognized body that provides, for common and repeated use, rules, guidelines or characteristics for activities or their results, aimed at the achievement of the optimum degree of order in a given context”.
There are several different types of standards. Basically, standards include requirements and/or recommendations in relation to products, systems, processes or services. Standards can also be a way to describe a measurement or test method or to establish a common terminology within a specific sector.
European Norms (ENs) are documents that have been ratified by one of the three European Standardization Organizations (ESOs), CEN, CENELEC or ETSI; recognized as competent in the area of voluntary technical standardization in line with EU Regulation 1025/2012.
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An EN (European Standard) “carries with it the obligation to be implemented at national level by being given the status of a national standard and by withdrawal of any conflicting national standard”.
Therefore, a European Standard (EN) automatically becomes a national standard in each of the 34 CEN-CENELEC member countries. Standards are voluntary which means that there is no automatic legal obligation to apply them. However, laws and regulations may refer to standards and even make compliance with them compulsory.
The International Standardization Organization (ISO), through its TC67 and TC8 sub-committees, on materials, equipment and offshore structures for petroleum, petrochemical and Managing Liquefied Natural Gas Risks in the Marine Industrynatural gas industries and Ships and Marine Technology, respectively, have been responsible for a large part of the LNG related standards that have been published, with relevance to LNG as fuel, small scale developments and bunkering. CEN, the European equivalent to ISO, has developed and published in parallel important standards for LNG equipment and safety. These are referred as EN/ISO standards.

Fig. 1 Development of ISO instruments – Technical Standards and International Standards – The diagram allows to see that the International Standard, following the TC/SC Route, comes as a natural continuation, following the TC/SC route
TC67 has developed ISO/TS 18683, Guidelines for systems and installations for supply of LNG as fuel to ships, whilst TC8 has recently finalized EN ISO 20519.
Table 1, below, lists the standards applicable to LNG (Liquefied Natural Gas) as FuelLNG as fuel, bunkering, and small scale LNG installations, considered relevant to equipment, safety and procedures in the context of LNG bunkering.
| Table 1. International Standards on LNG as fuel (ISO, IEC, CEN) | |||
|---|---|---|---|
| Title | Responsible | Type | Scope |
| EN STANDARDS | |||
| EN 1160 General characteristics of liquefied natural gas | CEN | European Norm | (replaced by EN ISO 16904) |
| EN 1473:2017 – Installation and equipment for liquefied natural gas – Design of onshore installations | CEN | European Norm | Design onshore LNG installations with LNG storage > 200 t |
| For large storage facilities, EN 1473 is the prevailing standard. This standard is based on a risk assessment approach. According to the scope this standard covers all kinds of LNG storage but is limited to atmospheric storage tanks. The standard is valid for LNG storage above 200 t. Pressurized intermediate storage tanks are excluded from this standard, as well as satellite plants with a storage capacity of less than 200 t, which are covered by EN 13645. | |||
| Standard valid for plants with LNG storage at pressure lower than 0,5 bar and capacity above 200 t and for the following plant types: | |||
| LNG liquefaction installations (plant); | |||
| LNG regasification installations (plant); | |||
| Peak-shaving plants; | |||
| The fixed part of an LNG bunker station. | |||
| EN 1474-1 – Design and testing of marine transfer systems. Design and testing of transfer arms | CEN | European Norm | (replaced by EN ISO 16904) |
| EN 1474-2 – Design and testing of marine transfer systems. Design and testing of transfer hoses | CEN | European Norm | Installation and equipment for liquefied natural gas. Design and testing of marine transfer systems. |
| EN 1474-3 – Design and testing of marine transfer systems. | Design, minimum safety requirements and inspection and testing procedures | ||
| Loading and unloading devices, Liquefied natural gas, Natural gas, Petroleum products, Loading (materials handling), Tankers, Ships, Design, Safety measures, Risk assessment, Equipment safety, Safety devices, Alarm systems, Control systems, Inspection, Performance testing. | |||
| EN 12065 – Testing of foam concentrates of extinguishing powders used on LNG fires | CEN | European Norm | Installations and equipment for liquefied natural gas. Testing of foam concentrates designed for generation of medium and high expansion foam and of extinguishing powders used on liquefied natural gas fires. |
| Flame retardants, Foams, Particulate materials, Concentrates, Fire retardants, Test equipment, Expansion (deformation), Testing conditions, Efficiency, Reports, Fire tests, Compatibility, Performance testing, Fire extinguishers. | |||
| EN 12066 – Testing of insulating linings for liquefied natural gas impounding areas | CEN | European Norm | Thermal insulation, Linings (containers), Test specimens, Test equipment, Dimensions, Thickness, Evaporation, Water-absorption tests, Mathematical calculations |
| EN 12308 – Suitability testing of gaskets designed for flanged joints used on LNG piping | CEN | European Norm | Installations and equipment for LNG. Suitability testing of gaskets designed for flanged joints used on LNG piping |
| Gas storage, Thermal insulation, Linings (containers), Test specimens, Test equipment, Dimensions, Thickness, Evaporation, Water-absorption tests, Mathematical calculations | |||
| EN 12838 – Suitability testing of LNG sampling systems | CEN | European Norm | Installations and equipment for liquefied natural gas. Suitability testing of LNG sampling systems. |
| Sampling equipment, Sampling methods, Gas analysis, Gas chromatography, Pressure testing, Flow measurement, Thermal testing, Test equipment, Performance testing, Capability approval, Physical properties of materials, Accuracy, Classification systems, Measuring instruments, Measurement characteristics, Mathematical calculations, Control samples, Statistical methods of analysis. | |||
| EN 13463-1 – Non electric equipment for use in potentially explosive atmospheres | CEN | European Norm | Standard with requirements for non-electrical equipment for use or located in potentially explosive atmospheres. |
| EN 13645 – Installation and equipment for liquefied natural gas – Design of onshore installations 5 t and 200 t | CEN | European Norm | Design onshore LNG installations with LNG storage capacity 5 – 200 t |
| It complements EN 1473, covering smaller scale storage LNG installations. | |||
| This standard only deals with pressurized vessels (above 0,5 barg). | |||
| EN 13766:2010 – Thermoplastic multi-layer (non- vulcanized) hoses and hose assemblies for the transfer of liquid petroleum gas and liquefied natural gas – Specification | CEN | European Norm | Requirements for two types of thermoplastic multi-layer (non-vulcanized) transfer hoses and hose assemblies for carrying liquefied petroleum gas and liquefied natural gas. |
| EN 14620:2006 – Design and manufacture of site built, vertical, cylindrical, flat-bottomed steel tanks for the storage of refrigerated, liquefied gases with operating temperatures between 0 °C and -165 °C | CEN | European Norm | This European Standard is a specification for vertical, cylindrical tanks, built on site, above ground and of which the primary liquid container is made of steel. The secondary container, if applicable, may be of steel or of concrete or a combination of both. The maximum design pressure of the tanks covered by this European Standard is limited to 500 mbar. |
| ISO STANDARDS | |||
| ISO/DTS 16901 – Guidance on performing risk assessment in the design of onshore LNG installations including the Ship/Shore interface | ISO | ISO Technical Specification | Risk assessment for LNG facilities onshore and at shoreline (export & import terminals). |
| EN ISO 16903 – Characteristics of LNG, influencing the design, and material selection | ISO | International Standard | Guidance on the characteristics of liquefied natural gas (LNG) and the cryogenic materials used in the LNG industry. It also gives guidance on health and safety matters. It is intended to act as a reference document for the implementation of other standards in the liquefied natural gas field. It is intended as a reference for use by persons who design or operate LNG facilities. |
| EN ISO 16904 – Design and testing of LNG marine transfer arms for conventional onshore terminals | ISO | International Standard | Specifies the design, minimum safety requirements and inspection and testing procedures for liquefied natural gas (LNG) marine transfer arms intended for use on conventional onshore LNG terminals, handling LNG carriers engaged in international trade. It can provide guidance for offshore and coastal operations. It also covers the minimum requirements for safe LNG transfer between ship and shore. |
| Although the requirements for power/control systems are covered, this International Standard does not include all the details for the design and fabrication of standard parts and fittings associated with transfer arms. | |||
| ISO 16904:2016 is supplementary to local or national standards and regulations and is additional to the requirements of ISO 28460. | |||
| ISO/AWI TR 18624 – Guidance for conception, design and testing of LNG storage tanks | ISO | International Standard | This guideline is under development by the ISO/TC67, but is still in preparatory stage. More specific information about the content is not yet available at the time of writing. |
| ISO/TS 18683 – Guidelines for systems and installations for supply of LNG as fuel to ships | ISO | ISO Technical Specification | ISO/TS 18683:2015 gives guidance on the minimum requirements for the design and operation of the LNG bunkering facility, including the interface between the LNG supply facilities and receiving ship as shown in Figure 1. |
| ISO/TS 18683:2015 provides requirements and recommendations for operator and crew competency training, for the roles and responsibilities of the ship crew and bunkering personnel during LNG bunkering operations, and the functional requirements for equipment necessary to ensure safe LNG bunkering operations of LNG fuelled ships. | |||
| It covers LNG bunkering from shore or ship LNG supply facilities, as shown in Figure 1 and described in Clause 4, and addresses all operations required such as inerting, gassing up, cooling down, and loading. | |||
| Aspects covered by ISO/TS 18683 that are not in EN ISO 20519: | |||
| Risk assessment for SIMOPS; | |||
| Risk Criteria. | |||
| EN ISO 20088-1 – Determination of the resistance to cryogenic spillage of insulation materials – Part 1: Liquid phase | ISO | International Standard | Describes a method for determining the resistance to liquid cryogenic spillage on cryogenic spillage protection (CSP) systems. It is applicable where CSP systems are installed on carbon steel and will be in contact with cryogenic fluids. |
| Liquid nitrogen is used as the cryogenic medium since it has a lower boiling point than liquid natural gas or liquid oxygen and it is not flammable. Additionally, it can be safely used for experiment. | |||
| Future parts of the standard will cover vapour phase and jet exposure conditions. | |||
| The test laboratory is responsible to conduct an appropriate risk assessment according to local regulation in order to consider the impact of liquid and gaseous nitrogen exposure to equipment and personnel. | |||
| EN ISO 20519 – Specification for bunkering of liquefied natural gas fuelled vessels | ISO | International Standard | Requirements for LNG bunkering transfer systems and equipment used to bunker LNG fuelled vessels, including equipment, operational procedures, training and qualifications of personnel involved. |
| ISO 20519:2017 sets requirements for LNG bunkering transfer systems and equipment used to bunker LNG fuelled vessels, which are not covered by the IGC Code. | |||
| This document includes the following five elements: | |||
| a) hardware: liquid and vapour transfer systems; | |||
| b) operational procedures; | |||
| c) requirement for the LNG provider to provide an LNG bunker delivery note; | |||
| d) training and qualifications of personnel involved; | |||
| e) requirements for LNG facilities to meet applicable ISO standards and local codes. | |||
| ISO/TS 17177 – Guidelines for the marine interfaces of hybrid LNG terminals | ISO | International Standard | ISO/TR 17177:2015 provides guidance for installations, equipment and operation at the ship to terminal and ship to ship interface for hybrid floating and fixed LNG terminals that might not comply with the description of “Conventional LNG Terminal” included in ISO 28460. |
| It is intended to be read in conjunction with ISO 28460 to ensure the safe and efficient LNG transfer operation at these marine facilities. | |||
| This standard also addresses high pressure natural gas (HPNG) at the transfer interface at facilities where liquefaction or regasification is undertaken, but does not describe requirements for the process plant generally forming part of the terminal facility. | |||
| These guidelines are based around facilities that are currently in operation or under development. | |||
| ISO 28460 – Standard for installation and equipment for LNG – Ship to shore interface and port operations | ISO | International Standard | Onshore LNG terminals and LNG carriers. |
| ISO 28460:2010 specifies the requirements for ship, terminal and port service providers to ensure the safe transit of an LNG carrier through the port area and the safe and efficient transfer of its cargo. | |||
| ISO 10976:2015 – Refrigerated light hydrocarbon fluids – Measurement of cargoes on board LNG carriers | ISO | International Standard | Describes the steps needed to properly measure and account for the quantities of cargoes on liquefied natural gas (LNG) carriers. This includes, but is not limited to, the measurement of liquid volume, vapour volume, temperature and pressure, and accounting for the total quantity of the cargo on board. This International Standard describes the use of common measurement systems used on board LNG carriers, the aim of which is to improve the general knowledge and processes in the measurement of LNG for all parties concerned. This International Standard provides general requirements for those involved in the LNG trade on ships and onshore. |
| ISO 15970:2008 – Natural gas – Measurement of properties – Volumetric properties: density, pressure, temperature and compression factor | ISO | International Standard | ISO 15970:2008 gives requirements and procedures for the measurement of the properties of natural gas that are used mainly for volume calculation and volume conversion: density at reference and at operating conditions, pressure, temperature and compression factor. |
| Only those methods and instruments are considered that are suitable for field operation under the conditions of natural gas transmission and distribution, installed either in-line or on-line, and that do not involve the determination of the gas composition. ISO 15970:2008 gives examples for currently used instruments that are available commercially and of interest to the natural gas industry. | |||
| ISO 18132-1:2011 – Refrigerated hydrocarbon and non-petroleum based liquefied gaseous fuels – General requirements for automatic tank gauges – Part 1: Automatic tank gauges for liquefied natural gas on board marine carriers and floating storage | ISO | International Standard | ISO 18132-1:2011 establishes general principles for the accuracy, installation, calibration and verification of automatic tank gauges (ATGs) used for custody transfer measurement of liquefied natural gas (LNG) on board an LNG carrier or floating storage. |
| The LNG described in ISO 18132-1:2011 is either fully refrigerated (i. e. at the cryogenic condition), or partially refrigerated, and therefore the fluid is at or near atmospheric pressure. | |||
| ISO 23251:2006 – Petroleum, petrochemical and natural gas industries – Pressure – relieving and depressuring systems | ISO | International Standard | ISO 23251:2006 is applicable to pressure-relieving and vapour-depressuring systems. Although intended for use primarily in oil refineries, it is also applicable to petrochemical facilities, gas plants, liquefied natural gas (LNG) facilities and oil and gas production facilities. The information provided is designed to aid in the selection of the system that is most appropriate for the risks and circumstances involved in various installations. |
| ISO 31000:2009, Risk management – Principles and guidelines | ISO | International Standard | ISO 31000:2009, Risk management – Principles and guidelines, provides principles, framework and a process for managing risk. It can be used by any organization regardless of its size, activity or sector. |
| ISO 31000 cannot be used for certification purposes, but does provide guidance for internal or external audit programmes. | |||
| ISO 17776:2016 – Petroleum and natural gas industries – Offshore production installations – Major accident hazard management during the design of new installations | ISO | International Standard | ISO 17776:2016 describes processes for managing major accident (MA) hazards during the design of offshore oil and gas production installations. It provides requirements and guidance on the development of strategies both to prevent the occurrence of MAs and to limit the possible consequences. It also contains some requirements and guidance on managing MA hazards in operation. |
| ISO/IEC Guide 73 Risk Management – Vocabulary | ISO/IEC | International Standard | ISO Guide 73:2009 provides the definitions of generic terms related to risk management. It aims to encourage a mutual and consistent understanding of, and a coherent approach to, the description of activities relating to the management of risk, and the use of uniform risk management terminology in processes and frameworks dealing with the management of risk. |
| IEC 31010:2009, Risk management – Risk assessment techniques | IEC/ISO | International Standard | IEC 31010:2009 is a dual logo IEC/ISO, single prefix IEC, and supporting standard for ISO 31000 and provides guidance on selection and application of systematic techniques for risk assessment. This standard is not intended for certification, regulatory or contractual use. |
| IEC STANDARDS | |||
| IEC 60092-502 Electrical installations in ships – Tankers – Special features | IEC | International Standard | This part of IEC 60092 summarizes the present IMO electrical requirements giving in a single publication details of suitable measures regarding the explosion protection of electrical equipment, in particular for tankers. |
| IEC 60079-10-1:2015 – Explosive atmospheres – Part 10-1: Classification of areas – Explosive gas atmospheres | IEC | International Standard | Standard concerned with the classification of areas where flammable gas or vapour hazards may arise and may then be used as a basis to support the proper selection and installation of equipment for use in hazardous areas. It is intended to be applied where there may be an ignition hazard due to the presence of flammable gas or vapour, mixed with air. |
| IEC 61508:2010 Functional safety of electrical/ electronic/programmable electronic safety-related systems – Parts 1 to 7 | IEC | International Standard | IEC 61508 is the international standard for electrical, electronic and programmable electronic safety related systems. It sets out the requirements for ensuring that systems are designed, implemented, operated and maintained to provide the required safety integrity level (SIL). |
| CESNI STANDARDS | |||
| CESNI Standard ES-TRIN 2015/1 – European standard laying down technical requirements for inland navigation vessels | CESNI | European Inland Navigation Standard | Contains provisions on inland navigation vessel construction, arrangement and equipment, special provisions for certain categories of vessel such as passenger vessels, pushed convoys and container vessels, as well as instructions on how to apply the technical standard. ES-TRIN also incorporates the new requirements governing the use of liquefied natural gas as a fuel (LNG). |
| In order to ensure consistency of two existing legal regimes for technical requirements for inland navigation vessels (Rhine and EU) it is necessary to provide the same standards. Both EU law (Directive (EU) 2016/1629) and CCNR Regulation will be referring to ES-TRIN standards delivered by CESNI from 7 October 2018. | |||
| In July 2017, the new edition 2017/1 of ES-TRIN was published. The CCNR and EU intend to enact ES-TRIN 2017/1 in a coordinated way, with effect from 07 October 2018, by means of a reference in their respective legislative frameworks. | |||
Other relevant standards are under preparation (At the date of release for the present of source):
- https://ulianovauto.ru/o-nas/ Bunker connectors = QC/DC (Marine LNG fuel bunkering quick connect/disconnect coupling), following the functional requirements outlined by ISO 20519, but taking the work up to the level of International Standard. NWIP ISO 21903.
- LNG metering – Guidance for the calibration, installation and use of flow meters for LNG and other refrigerated hydrocarbon fluids, under development as a new item proposal NWIP ISO 21903 accepted 28/09/2016.
- LNG quality.
From all the standards listed in the table 1, two particular documents are summarized below, accounting for their relevance in the context of LNG bunkering operations. They are ISO/TS 18683 and EN ISO 20519. Both standards are similar in scope and some parts of ISO/TS 18683 can even be found in the most recent standard EN ISO 20519. They both focus on the LNG bunkering interface, excluding the LNG supplier system/infrastructure, and the receiving ship, establishing the division line at the flanges from both sides (see figure 2, below).

It is relevant to mention, in the context of this Guidance, that given the normal course of ISO publications life-cycle, ISO/TS 18683 is likely to be repealed in the near future, leaving the necessary space for the International Standard (EN ISO 20519) as the reference specification for LNG bunkering.
EN ISO 20519
Specification for bunkering of liquefied natural gas fuelled vessels (published 10-2-2017).

1 – Scope boundary; 2 – Automatic and manual ESD valve; 3 – ESD junction box; 4 – Insulation flange; 5 – Emergency release coupling; 6 – QC/DC – Quick Connect/Disconnect Coupling; 7 – Ship/shore or ship/ship ESD link; 8 – Loading system (systems include; vessel to vessel transfer arms, articulated rigid piping); 9 – Vapour return system
ISO 20519:2017 is the most recent standard of relevance to LNG bunkering, setting requirements for transfer systems and equipment used to bunker LNG fuelled vessels, which are not covered by the IGC Code. This document includes the following five elements:
a) hardware: liquid and vapour transfer systems;
b) operational procedures;
c) requirement for the LNG provider to provide an LNG bunker delivery note;
d) training and qualifications of personnel involved;
e) requirements for LNG facilities to meet applicable ISO standards and local codes.
The scope of ISO 20519 is presented in figure 2, above.
An important point to note in figure 2, above, is the inclusion of the vapour return as an important point covered by the functional requirements in EN ISO 20519. It is an important point to consider that during bunkering of LNG vapour management is fundamental. A part of the LNG delivered will evaporate due to the heat transfer in the bunkering line and fuel piping onboard, down to the receiving tank. To manage pressure build-up inside the tank, it is important to address the need to return vapour from that same tank during the LNG bunkering process – standards and rulesbunkering process. Venting is not an operational option, and should only be considered in emergency.
It will be interesting: LNG (Liquefied Natural Gas) as Fuel
The scope of both EN ISO 20519 and ISO/TS 18683 is important to understand how the regulatory frame should be composed to shape a consistent and coherent legal frame for LNG bunkering. Being strictly scoped to the LNG bunkering interface and operations, both standards exclude coverage of any mobile LNG bunkering units/transport or even of any elements related to the ship side. The challenge is to provide the best compatibility instrument between all involved parties and relevant elements.
A particular element where the scope may be extended, covering aspects related to other elements is the Risk Assessment. In fact, in regards to Safety evaluation the scope cannot be defined so rigidly and all the elements (truck, bunker barges, receiving ship, onsite storage, etc., need to be assessed as a whole, integrated in the same Bunkering risk on Liquefied natural gas ships assessment and safety zonesrisk assessment, both from an hazard identification perspective and from risk evaluation.
The following parts are covered by EN ISO 20519:
- Bunker vessel requirements.
- Receiving Vessel requirements.
- Facility requirements.
- Transfer equipment requirements (list of standards applicable to the transfer system components).
- ESD/ERS systems (Emergency Release System, including requirement for Emergency Release Coupling, ERC). Outline of functional requirements for system components.
- Specific Requirements for:
- System Support.
- Hoses, corrugated metallic or composite.
- Transfer Arms.
- Bunkering Connections.
- Insulation Flange.
- Fall arrest.
- Transfer system design analysis.
- Maintenance/Maintenance manual.
- Mooring.
- Communication in preparation for a transfer:
- Information that the BSO shall provide to the RSO, for each transfer and, specifically, for the first transfer.
- Information that the RSO shall provide to the BSO, for each transfer and, specifically, for the first transfer.
- Risk Assessment:
- Conditions Considered for the Risk Assessment.
- Methodology.
- Acceptable bunkering parameters.
- Vessel Safety Assessment.
- Transfer Procedures, including aspects related to the PICs, manifold and hose watch during transfer, references to CCTV, check-lists, PPE.
- Management Systems. Conformance with EN ISO 20519, through management objective in one of the following accredited management systems:
- ISO 9001.
- ISO 14001.
- ISM.
- ISO/TS 29001.
- API Spec Q1.
- Management systems for transfer equipment manufacturers.
- Vessel personnel training requirements:
- Minimum requirements: STCW, IGC and IGF provisions as applicable.
- Additional training requirements for personnel involved in bunkering operations on vessels (additional to requirements in STCW, ADR, ADN). For personnel with assigned duties to LNG bunkering:
- Onboard a vessel.
- Port.
- Documentation of training.
- List of relevant records and documents that should be maintained for compliance with EN ISO 20519:
- Transfer System analysis.
- RSO vessel certification.
- BSO vessel certification.
- ISO 20519 compliance document for port facilites, vehicles, portable tanks.
- Listing of maintenance and inspection of selected equipment (all the equipment listed in the transfer system).
- Copies of all completed check-lists.
- Training Records.
- Copies of the Risk Assessment.
- LNG Bunker Procedures Manual:
- Bunkering parameters for the transfer system described, BFO and (to be kept by all parties adhering to EN ISO 20519).
- Minimum Check-list template included for:
- Planned Operations Checks (to be filled within 48 h in advance).
- Pre-Operational Checks (Pre-Bunkering check-list) – vessel-to-vessel.
- LNG Transfer (Checks immediately before transfer of LNG) – tank-to-tank.
- SIMOPS.
- Post-bunkering (vessel-to-vessel).
- Criteria and methodology for Control Zones definition (same approach as ISO/TS 18683).
EN ISO 20519 is referred throughout this Guidance as the standard that should serve as a basis for certification, accreditation and quality assurance of all stakeholders. The EN notation is here essential to ensure that, at least in the EU, the standard is incorporated by all EU Member States as a national standard.
This standard represents an instrument of direct support to the IGF Code, providing the frame for implementation of IGF Section 18.4 provisions on bunkering operations.
As mentioned above, this International Standard shares some significant parts that were already known from ISO/TS 18683 (e. g. the parts on determination of safety zones, transfer system functional requirements, and requirements for training and documentation). It is important to note that these two ISO documents currently co-exist in the frame of LNG Bunkering. It is typical of the ISO development process for a Technical Specification to be developed as a first step towards an International Standard. In this regard, it has been suggested that the ISO/TS may be withdrawn at a later stage. For the purposes of this Guidance, the two instruments are considered valid and complementary. In the next page, ISO 18683 is summarized.
ISO/TS 18683
ISO/TS 18683 – Guidelines for systems and installations for supply of LNG as fuel to ships (Technical Specification published 15-1-2015).

ISO/TS 18683:2015 gives guidance on the minimum requirements for the design and operation of the LNG bunkering facility, including the interface between the LNG supply facilities and receiving ship. It provides requirements and recommendations for operator and crew competency training, for the roles and responsibilities of the ship crew and bunkering personnel during LNG bunkering operations, and the functional requirements for equipment necessary to ensure safe LNG bunkering operations of LNG fuelled ships. It covers LNG bunkering from shore or ship LNG supply facilities, and addresses all operations required such as inerting, gassing up, cooling down, and loading.
The objective of this Technical Specification is to provide guidance for the planning and design of the following and thereby ensuring that an LNG fuelled ship can refuel with a high level of safety, integrity, and reliability:
- bunkering facility;
- ship/bunkering facility interface;
- procedures for connection and disconnection;
- monitoring procedures during bunkering;
- emergency shutdown interface;
- LNG bunkering process control.
The LNG bunkering interface is for the first time scoped and defined in ISO/TS 18683, being defined as the area of LNG transfer and includes manifold, valves, safety and security systems and other equipment, and the personnel involved in the LNG bunkering operations.
The ISO/TS 18683:2015 thus defines the overall philosophies of designs and operations relevant to LNG bunkering and suggests a list of 24 functional requirements, whilst addressing safety by outlining 3 (three) layers of defence to ensure safe operations. The 3 layers of defence are defined as follows:
The structure of functional requirements, summarized in Annex C of ISO/TS 18683, and transcribed in table 2 below, defines the basic functions that need to be accomplished by any designed solution for LNG bunkering, both in terms of equipment and procedures.
| Table 2. ISO/TS 18683:2015 Functional Requirements | |||
|---|---|---|---|
| Functional Requirement ISO/TS 18683 | Short description | Relevant Section in ISO/TS 18683 | Relevant Section in EN ISO 20519 |
| F1 | Compatibility check between supplier and ship | 8.3 | 5.3, 5.4 |
| F2 | Can the system be commissioned and operated (purged and inerted) without release of LNG or natural gas to the atmosphere? | 8.4, 9.2 (Table 1, Table 2) | 5.5.4, 6.5.9 |
| F3 | Is the system closed and leak tested prior to bunkering? | 8.4, 9.2 (Table 1, Table 2) | 6.5.5 |
| F4 | Design should reflect operating temperature and pressure and be in accordance with recognized standards. | 8.5.2, 9.2 (Table 1, Table 2), Annex G | 5.3.2, 5.3.3 |
| F5 | The design shall reflect the required operational envelope (motions, weather, visibility). | 8.5.2, 9.2 (Table 1, Table 2) | 5.6(k), 5.4, 5.7.1 |
| F6 | The transfer system shall be capable of being drained, de-pressurized and inerted before connections and disconnections are made. | 8.5.2, 9.2 (Table 1, Table 2), Annex G | 5.5.4, 5.6, 6.5.9 |
| F7 | The bunkering transfer system shall be designed to avoid trapped liquid. | 8.5.2, 9.2 (Table 1, Table 2) | No reference |
| F8 | Operating procedures shall be established and documented to define the bunkering process and to ensure that components and systems are operated in a safe way within their design parameters during all operational phases. For truck loading, the procedures will normally be defined for the truck operation but need to be aligned to specific ship requirements. | 8.5.2, 9.2 (Table 1, Table 2) | Section 6 No specific reference to truck-to-ship operation 6.5.1 |
| F9 | All systems and components shall be maintained and tested according to, as a minimum, vendor recommendation to maintain their integrity. | 8.5.2, 9.2 (Table 1, Table 2) | 5.8 |
| F10 | An organizational plan shall be prepared and implemented in operational plans and reflected in qualification requirements. | 8.5.2, 9.2 (Table 1, Table 2) | 6.5 Section 9 (LNG Bunkering Procedures Manual) |
| F11 | Operating procedures shall include a checklist to be completed and signed by both parties prior to the commencement of bunkering (this may serve as a bunkering permit as required by authorities). | 8.5.2, 9.2 (Table 1, Table 2) | 6.5.3, 6.5.7 |
| F12 | Emergency equipment and personnel shall be mobilized in accordance with the emergency response plan. | 8.5.2, 9.2 (Table 1, Table 2) | 6.5.1, Section 9 (LNG Bunkering Procedures Manual) |
| F13 | Operating procedures shall not be applied as an alternative to a particular fitting, material, or item of equipment. | 8.5.2, 9.2 (Table 1, Table 2) | No reference |
| F14 | Minimize the likelihood of igniting potential LNG releases. This is accomplished by elimination of ignition sources in classified areas and by controlling activities in the proximity of the bunkering operation. No smoking signs. | 8.5.3 | Annex B – Controlled Zones |
| F15 | Elimination of the potential spark or high currents from static or galvanic cells when the bunkering system is connected or disconnected. | 8.5.3 | 5.5.6 |
| F16 | Effective detection of release of LNG and natural gas. Selection of sensors and sensors location should consider possible presence of mist and fog that might mask the leak. Manual detection may be accepted for continuously monitored short duration operations Manual detection in areas where water mist can occur shall not be accepted. | 8.5.3 | 6.5.2.2 6.5.2.3 Relevance is given to hose and manifold watch, including CCTV. |
| F17 | The transfer operation shall be capable of being stopped safely and effectively without release of liquid or vapour, either manually or by an ESD signal. | 8.5.3, 9.2 (Table 1, Table 2) | 5.4.1.1, 5.4.1.2, 5.4.2 |
| F18 | The transfer system shall be provided with an ERS (emergency release system) or breakaway coupling, to minimise damage to the transfer system in case of ships drift or vehicle movement. This should be designed for minimum release of LNG if activated. The ERS may be linked to the ESD system (where this may be referred to as ESD 2). | 8.5.3, 9.2 (Table 1, Table 2) | 5.4.1, 5.4.1.1 |
| F19 | The release of LNG or cold vapour should not lead to an escalation due to brittle fractures of steel structure. | 8.5.3 | Reference in Part A Check-List – Annex A |
| F20 | Personnel shall use PPE (personnel protective equipment) as appropriate for the operations. | 8.5.3 | 6.5.10 |
| F21 | A safety zone shall be implemented around the bunkering operation into which only essential personnel shall have access. | 8.5.3 | Annex-B |
| F22 | Activities in the area adjacent to the bunkering operation shall be controlled to reduce possible ignition sources. | 8.5.3 | 6.3.5 Part B Check-list – Annex A |
| F23 | Contingency plan shall be in place. | 8.5.4 | No exact reference. Section 9 (LNG Bunkering Procedures Manual) |
| F24 | Copies of the plan shall be communicated to all parties involved in the bunkering operation including the planned emergency response team and be part of the training program. This should be practiced at regular intervals both as “table top” and practical exercises. | 8.5.4 | The plan can be scoped within the LNG Bunker Procedures Manual (part of Section 9) |
As it can be seen in the table above, both ISO/TS 18683 and EN ISO 20519 share provisions that relate to the same functional requirements outlined in the first Technical Specification. There is however a difference that should be noted.
ISO/TS 18683 is more a standard to assist in the design of the LNG Bunkering solution, whilst EN ISO 20519 is more focused on the operational aspects of LNG Bunkering. Functional requirements for equipment are addressed in both.
The most significant difference between the two documents is the contents related to the safety philosophy and provisions on Risk Assessment that are in ISO/TS 18683, but not in EN ISO 20519. Whilst the first document, as a technical specification, list requirements for Risk Assessment, of a more prescriptive nature, the second outlines very briefly the objective for the Risk Assessment, listing the minimum conditions that should be observed and documented for that exercise. In actual terms EN ISO 20519 does not prescribe any methodology, nor does it explain which approach should be followed for the Risk Assessment. It leaves room, in this way, for Risk Assessments to be developed in strict response to requirements from specific national/local competent authorities. EN ISO 20519 paragraph 6.3.4 a) If the risk assessment is being performed to meet a requirement set by national or local authorities that have jurisdiction over the safety and security where the bunkering operation will take place, the assessment methodology used should conform to requirements set by the authorities.x On the other hand, ISO/TS 18683 requires risk assessments to be agreement with recognized standards, such as ISO 31010, ISO 17776, and ISO 16901 ISO/TS 18683 section 7.1.x, describing further both “qualitative” and “quantitative” risk assessment approaches, listing for each one the activities they should be comprised of, the study basis and the elements that should be present the different approaches.
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The Risk Assessment approaches, as described in ISO/TS 18683, together with the concepts outlined for risk matrix and for possible risk criteria to adopt, provide examples that, together with ISO 31010, ISO 17776 and ISO 16901, can be considered as relevant references in the context of risk assessment of bunkering LNG as fuel for ships. Notwithstanding this, the matrix given in Annex A, Figure A-1 should deserve careful reflection before its use in the context of bunkering LNG as fuel for ships. Due to:
- little/insufficient experience of bunkering LNG as fuel for ships (let alone by a single operator);
- and a poor categorisation suitable to the estimation of high-consequence, low-probability events (especially as there is little experience) it would be better to simply state that examples of risk criteria are given and their applicability needs to be agreed with stakeholders.
Other industry best practice references, national safety legislation or others may also be relevant, especially with regards to the definition of the applicable risk criteria (Annex-A of ISO/TS 18683 provides only an example which is non-binding or compulsory, even if the standard is made mandatory through any legal reference). As regards LNG bunkering, this technical specification remain the reference for the main risk assessment concepts, not outlined as a standard but more as a technical frame that should be taken into account when preparing, conducting, reporting and evaluating risk studies that are required as support tools to the development of LNG bunkering solutions.
The above considerations, in the context of ISO/TS 18683, are relevant to underline that EN ISO 20519 should not be regarded as a replacement for this technical specification, or as its evolution. ISO/TS 18683 is still valid, especially with regards to the aspects related to Risk Assessment, with a very significant list of possible hazardous scenarios that need to be considered, with an outline of minimum requirements and methodologies explained. EN ISO 20519, on the same subject of risk assessment, takes the route of suggesting that the risk assessment methodology should be the one prescribed by the competent/local authority where the permitting is being sought from. This is also found to be highly relevant but leading to considerations on how prepared are competent authorities to prescribe actual methodologies or, even, in some cases, to have clearly defined risk criteria.
- Properties and behaviour of LNG.
- Description and hazards of LNG.
- Potential hazardous situations associated with LNG transfer.
- Composition of LNG as a bunker fuel.
- Objectives.
- General Safety Principles.
- Approach.
- Qualitative Risk Assessment:
- Main steps.
- Study basis.
- HAZID.
- Determination of Safety Zones.
- Determination of Security Zones.
- Reporting.
- Quantitative Risk Assessment:
- Main steps.
- Study basis.
- HAZID.
- QRA calculation.
- Frequency Analysis.
- QRA Report.
- Design and operation basis.
- Compatibility between supplier and ship.
- Prevention of releases of LNG or natural gas to the atmosphere.
- Safety.
- Functional requirements to reduce risk of accidental release of LNG and natural gas.
- Requirements to contain hazardous situations.
- Emergency preparedness.
Guidelines
The present section provides an overview of available guidelines on LNG bunkering that have been the main support references in the development of LNG bunkering solutions. ISO/TS 18683 and EN ISO 20519 are included.
A summary of existing guidelines and best practice references is included in table 3 below, representing what are today the best industry-recognized references to assist LNG bunkering operations.
The table above includes a list of standards, guidelines and references containing requirements and best practices regarding equipment, safety, procedures and other aspects related to LNG bunkering.
They are the best references today where industry experience has resulted in a comprehensive collection of provisions to support the safe development of LNG bunkering facilities and operations, providing the framework for efficient and safe bunkering. They put forward requirements with regard to safety management, operational procedures and minimum safeguards to prevent accidents and/or mitigate the consequences. A structured way to discuss the quality and the completeness of the LNG bunkering guidelines listed above has been used in the EU LNG Study, by DNV-GL, where the different categories of items are structured in a systematic approach. The approach used is the Structured What-If Checklist (SWIFT) technique (DNV-GL trademark). The SWIFT study technique has been developed as an efficient technique for providing effective hazards identification. SWIFT is a systems-oriented technique which examines systems, subsystems or activities.x
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The LNG Regulatory Framework International and European Maritime Safety OverviewLNG bunkering guidelines presented in Table 3 are now compared to assist PAAs whenever referring to existing guidance/best practice documents. Where and how complete the information can be found is the objective of the analysis and comparative exercise.
Table 4, below, lists and details the categories and criteria used to compare the different instruments.
| Table 4. Categories for comparison of LNG Bunkering Guidelines | ||
|---|---|---|
| Comparison Category | Summary descriptor | |
| Material Problems (MP) | This category is concerned with the potential hazards and the conditions that need to be maintained in order to safely store, handle and process the materials: LNG, nitrogen. This includes: | Flammability, Flash points |
| Potential for material instability | ||
| Static electrical charge build up and discharge (grounding/bonding) | ||
| Safe storage & transfer temperature & pressure | ||
| Exposure Limits – personal protective equipment requirements | ||
| Contamination from outside sources | ||
| Contamination through process connections | ||
| Mixing or settling hazards | ||
| External Effects or Influences (EE/I) | This category is intended to help identify the effect of outside forces or demand scenarios which might result in the development of some of the hazards identified during discussions of material problems (MP). Included might be natural phenomena, weather influences. Also to be considered are man-made random events such as arson, civil disturbances, or a nearby explosion which might in some way impact the operation. | |
| Operating Errors and Other Human Factors (OE&HF) | This category is related to every conceivable way to mis-execute the process as intended. It is important to remember that many operating errors are the result of inadequate training or poorly written or incomplete instructions. | |
| Analytical or Sampling Errors (A/SE) | This category is related to all potential analytical or sampling requirements or operations: | Sampling procedure is unsafe |
| Significance of analysis results not well understood by operator | ||
| Test results are delayed | ||
| Test results are incorrect | ||
| In-line analytical device out of calibration | ||
| Sample point left open or leaking | ||
| Equipment/Instrumentation Malfunction (E/IM) | This category is related to all potential significant mechanical and instrumentation failures. It is crucial to note of protective devices and systems which must remain operative if the various mechanical and human demands are to be prevented from causing a hazard. Protective system proof testing schedules should also be reviewed. | |
| Process Upsets of Unspecified Origin (PUUO) | This category is intended to be a “catch all” for additional demands. This category also should serve as a reminder that the materials and process conditions within a system or subsystem may be directly influenced by the conditions at the point of interface with other systems or subsystems. | |
| Utility Failures (UF) | This category is straightforward but care should be taken to note that external effects or influences (EE/I), analytical or sampling errors (A/SE), operating errors and other human factors (OE&HF) and electrical/instrumentation malfunction (E/IM) may directly cause a utility failure (UF) type hazard: | Power fails |
| Instrument air fails | ||
| Inert fails | ||
| Communications system fails | ||
| Fire system fails | ||
| Integrity Failure or Loss of Containment (IF/LOC) | This category should draw heavily upon all the preceding categories. Additional care concerning the accuracy and detail of the logical interaction of previous errors and/or failures with each other should be considered. Integrity failure or loss of containment (IF/LOC) hazards certainly can introduce some additional considerations such as normal and emergency venting. However, some combination of the demands and hazards previously identified will probably represent the major basis for those scenarios which could result. It should also be noted that tanks, lines, pumps and various other components need to be considered in this discussion, and the size of such failures should be specified (small leak, catastrophic failure, etc.) | |
| Emergency Operations (EO) | If the analysis of the ultimate effects of the various consequences relating to all the previous categories, new issues will rarely be discovered at this stage. It is, however, very important to consider emergency operations independently because errors or failures related directly to the emergency condition or emergency procedures may not have been readily apparent when the emergency was discussed in the context of the precipitating events. Possible escalation of minor situations during emergencies should also be evaluated. | |
| Environmental Release (ER) | The most obvious release will be that caused by integrity failure or loss of containment (IF/LOC). However, correctly functioning emergency vents, various mechanical failures and operating errors must also be considered. | |
Table 4, using the categories presented below, makes a comparison of topics addressed in the different procedures & guidelines (the IAPH checklist is not included in the table).
The level of detail of how these topics are addressed can differ significantly between the different documents. It is advisable therefore to use the published guidelines as a first informative resource to gain background on technology, equipment requirements and procedures. How the Guidelines, altogether, can be used will depend mainly on the following factors:
- Agreement between all parties involved (BSO, RSO, Terminal, Competent Authority(ies).
- Prescription of specific Guidelines by local regulations.
- Technology development.
Guidelines are also very different in nature. Whilst ISO/TS 18683 establishes functional requirements for equipment and procedural aspects, the SGMF Safety Guidelines for LNG bunkering are more of an operations guide, in support of operations control/management in the LNG bunkering interface. It is important to use the relevant guidelines for the relevant aspects of LNG bunkering. None of the instruments listed can be considered complete and, following the very nature of guidance documents, they aim to provide orientation in particular aspects of LNG bunkering equipment design, operations, competencies and training.
| Table 5. Guidelines on LNG Bunkering – Documents comparison | ||||||
|---|---|---|---|---|---|---|
| ISO TS 18683 | EN ISO 20519 | DNV GL RP | BV guidelines | ABS guidelines | SGMF guidelines | |
| General issues | ||||||
| general introduction& scope | × | × | × | × | × | × |
| bunkering scenarios/options/configurations | × | (1) | × | × | × | × |
| Material Problems (MP) | ||||||
| general safety | × | × | × | – | × | × |
| use of checklists | × | × | × | – | – | × |
| general risk management | × | – | × | – | – | × |
| safety and security zones, general | × | × | × | – | × | × |
| fire protection systems | – | (2) | × | × | × | × |
| ignition prevention | × | (2) | × | × | × | × |
| fire and gas detection | × | (2) | × | – | × | |
| safety zones requirements | × | × | × | × | × | × |
| personal protective equipment (PPE) | × | × | × | – | × | × |
| External Effects Or Influences (EE/I) | ||||||
| lighting/visibility conditions | – | (3) | × | × | – | × |
| weather conditions, operating envelope | × | × | – | × | – | × |
| Operating Errors And Other Human Factors (OE&HF) | ||||||
| roles & responsibilities general | × | – | × | – | × | × |
| person in charge definition | – | – | × | × | × | |
| training requirements | × | × | × | × | × | |
| port & authorities involvement/approval | (4) | (4) | × | × | – | × |
| specific supplier responsibilities | × | – | × | – | – | – |
| outline of LNG transfer procedure | × | × | × | × | × | × |
| specific instructions for LNG bunkering operations | × | × | × | × | – | × |
| ship & supplier compatibility | × | – | × | × | × | × |
| communication/language | × | × | × | × | × | × |
| documentation requirements | × | × | – | – | – | – |
| Analytical Or Sampling Errors (A/SE) | ||||||
| LNG bunker quantity & quality | × | – | × | – | × | (8) |
| Equipment/Instrumentation Malfunction (E/IM) | ||||||
| loading arms | – | – | × | – | – | – |
| bunkering hoses | – | – | × | × | – | – |
| bunker piping | – | – | – | × | – | × |
| Process Upsets Of Unspecified Origin (PUUO) | ||||||
| alarms | × | (5) | – | × | × | × |
| management of change | – | – | × | × | – | |
| specific design requirements | (6) | (6) | – | × | × | – |
| simultaneous operations (SIMOPS) | × | – | × | – | × | × |
| control of operations | × | × | × | – | – | × |
| Utility Failures (UF) | ||||||
| electrical insulation | × | – | × | – | × | × |
| specific purging instructions | – | – | × | – | × | × |
| Integrity Failure Or Loss Of Containment (IF/LOC) | ||||||
| guidance for development & design of bunkering facilities | × | × | × | – | – | – |
| risk assessment requirements | × | – | × | × | × | × |
| cryogenic protection | × | – | × | – | × | × |
| specific connection instructions | – | – | – | – | × | × |
| specific transfer instructions | × | × | × | × | × | × |
| Emergency Operations (EO) | ||||||
| emergency shut down and emergency release | × | × | × | × | × | × |
| testing of ERS and ESD | × | × | – | – | – | – |
| emergency response | × | – | × | × | × | × |
| Environmental Release (ER) | ||||||
| vapour management | – | (7) | × | × | – | × |
(1) EN ISO 20519 does not address specific bunkering scenarios/options/configurations. The provisions are considered to be applicable to all bunkering modes. The check-lists included in this standard are however only for ship-to-ship bunkering.
(2) Even though no specific provisions are included for fire safety, EN ISO 20519 includes requirements for emergency systems such as ESD or ERS. These can be considered relevant for protection against spill/accidental LNG release and, therefore, also relevant in fire and ignition prevention.
(3) Small reference to lighting and visibility in 6.2.3.
(4) Alignment with competent authority requirements mentioned.
(5) Only related to ESD.
(6) Only functional requirements.
(7) Vapour return is included.
(8) SGMF has specific guidance on Quality, Quantity and Custody.
Other References
Having listed high-level instruments in section “High Level Instruments”, International Standards in section “Standards” and Guidelines in section “Guidelines”, the present section includes further references considered relevant in the context of LNG bunkering. Table 6, below, includes a list of references which are considered important to either address the whole, or part, of the LNG bunkering process. Study reports, including relevant analysis and findings, national/local/port regulations, industry guidance on specific equipment or operational aspects, are some of the documents presented in the table.
| Table 6. Guidelines on LNG Bunkering – Documents comparison | |||
|---|---|---|---|
| Title | Responsible | Type | Scope |
| USCG Regulations and Policy letters | |||
| Title 33 Code of Federal Regulations (33 CFR 127) Parts 127 | US Federal Regulation | Regulation | This high level document includes regulation for LNG bunkering in all bunkering modes. |
| Waterfront facilities handling Liquefied Natural Gas and Liquefied Hazardous Gas | It includes requirements on: | ||
| Equipment | |||
| Operations | |||
| Maintenance | |||
| Training | |||
| Firefighting | |||
| Security | |||
| 49 CFR 19 – Liquefied Natural Gas Facilities: Federal Safety Standards (DOT) | US Federal Regulation | Regulation | This high level document includes regulation for LNG equipment and facilities. |
| CG-OES Policy Letter 01-17 – 14AUG17 | USCG | Policy Letter | USCG Operational & Environmental Standard (OES) Policy letter providing a structured approach for port authorities to address and authorize SIMOPS. Policy Letter to Port Authorities. |
| Guidance for Evaluating Simultaneous (SIMOPS) During Liquefied Natural Gas (LNG) Fuel Transfer Operations | |||
| CG-OES Policy Letter 02-15 (2015) Guidance related to Vessels and Waterfront Facilities Conducting Liquefied Natural Gas (LNG) Marine Fuel transfer (Bunkering) Operations | USCG | Policy Letter | Guidance to owners and operators of vessels and waterfront facilities intending to conduct LNG bunkering operations, and to Coast Guard Captains of the Ports (COTPs) who assess fuel transfer operations. |
| Minimum safety and security requirements for LNG fuel operations, providing guidance that may be used by Port Authorities assessing the different situations in LNG Bunkering. | |||
| CG-OES Policy Letter 01-15 (2015) Guidelines for Liquefied Natural Gas Fuel Transfer Operations and Training of Personnel of Vessels Using Natural Gas as Fuel | USCG | Policy Letter | Policy letter providing guidance regarding vessels that use natural gas as fuel and conduct LNG fuel transfer operations. It addresses fuel transfer operations and training of personnel working on US flagged or foreign vessels that use LNG as fuel and conduct LNG fuel transfer operations in waters subject to US jurisdiction. |
| USCG CG-521 Policy Letter 01-12 Equivalency Determination: Design Criteria for Natural Gas Fuel Systems | USCG | Policy Letter | Policy letter providing guidance regarding vessels that use natural gas as fuel and conduct. |
| Updated 12JUL17, incorporating aspects from the IGF Code, following its entry into force on 1JAN17 | |||
| LGC NCOE Field Notice 01-2015, CH-1 | LGC NCOE | Field Notice – Technical recommendation | Field notice (memorandum) to augment to the references: |
| – CG-OES Policy Letter 01-15 – Guidance for Liquefied Natural Gas Fuel Transfer Operations and Training of Personnel on Vessels using Natural Gas as Fuel | |||
| – CG-OES Policy Letter 02-15: Guidance Related to Vessels and Waterfront Facilities Conducting Liquefied Natural Gas (LNG) Marine Fuel Transfer (Bunkering) Operations. | |||
| Includes specific recommendations following field experience in LNG bunkering operations. | |||
| Focus on procedures, understanding of actual hazardous properties of LNG, training requirements. | |||
| LGC NCOE Field Notice 01-2017, on SIMOPS | GC NCOE | Field Notice – Technical recommendation | Recommended Process For Analysing Risk Of Simultaneous Operations (SIMOPS) During Liquefied Natural Gas (LNG) Bunkering |
| USCG NVIC No. 01-2011 – Guidance related to waterfront LNG facilities | US/USCG | Guidance | This circular from the Unites States Coast Guard provides guidance to an applicant seeking a permit to build and operate a shore side LNG terminal. It also includes information on assessing the suitability of waterways for LNG marine traffic. |
| Even though it is applicable to LNG terminals it offers a broad general example on how permitting process can be structured. It provides a good reference on best practice. | |||
| Industry Best Practice – Industry Guidance | |||
| Alleviation of Excessive Surge Pressures on ESD (recommended practice) | SIGTTO | Industry Recommended Practice | This paper provides practical guidance to operators, designers and engineers, of both liquefied gas ship and terminal loading and unloading systems, by enabling them to recognise the potential hazard of surge pressure. |
| Manifold recommendations for Liquefied Gas Carriers | SIGTTO | Industry Guidance | Developed by SIGTTO and OCIMF, these recommendations summarise the manifold arrangements and strainer guidelines for LPG and LNG carriers. The document’s aim is to promote improved safety and efficiency in operations and to assist in planning the position of loading and discharging facilities in new jetties. |
| Liquefied Gas Fire Hazard Management | SIGTTO | Industry Guidance | The Fire Hazard Management guidelines covers many aspects of the liquefied gas industry, including large refrigerated and smaller pressurised storage terminals, ships, cylinder filling plant and road and rail tanker loading racks. The development of these guidelines focuses on operational staff, such as plant supervisors and ships’ officers, who are involved in the handling of flammable liquefied gases. It will also be beneficial to fire officers and emergency planners who have liquefied gas instillations within their jurisdiction, or experience regular road or rail car traffic involving these products in their area. This publication has been compiled to provide readers with an insight into the design and operation of liquefied gas installations and the equipment essential to the safe and efficient functioning of such installations. |
| ESD Arrangements and linked ship to shore systems for Liquefied Gas Carriers | SIGTTO | Technical Note | A note produced (2009) solely due to clarify the functional requirements for ESD systems, primarily differences between the needs of the LNG industry and those of the LPG industry. |
| Proposals are presented for a standardised links to connect ship and terminal emergency shutdown (ESD) systems that are designed to communicate and initiate ESD of cargo transfer as safely and as quickly as possible. | |||
| LNG Transfer Arms and Manifold Draining, Purging and Disconnection Procedures | SIGTTO | Industry Guidance (also adopted as Policy Letter USCG) | Due to confusion and misunderstanding among some ship and jetty operators regarding safe conduct of this operations these guidelines have been prepared. This advice specifically pertains to terminals employing rigid transfer arms. (The basic principles are applicable for hose systems that may be used for LNG ship to ship transfer, but there will be differences in the detail.) |
| The safe transfer of Liquefied Gas in an offshore environment | OCIMF | Best practice document/ Guidance | This publication primarily addresses the inter-relation between a Floating-Production-Storage-Offloading (FPSO) unit and conventional gas tankers operating in a side by side mooring configuration. It includes recommendations for mooring equipment, considers mooring loads and operations, motions of the FPSO and gas tanker, station keeping, cargo transfer equipment and cargo transfer operations. |
| The Guidelines are primarily intended to familiarise Masters, ship operators, FPSO operators and project development teams with the general principles and equipment involved in LPG offloading activities between FPSOs and gas tankers. | |||
| Ship Inspection Report Programme | OCIMF | Inspection Format Guidance | OCIMF ship inspection report programme (SIRE) is developed for tanker and barge risk assessment. It is a tool launched in 1993, used by charterers, terminal operators and government bodies to assist in the assurance of vessel safety and to provide a standardized inspection format, with objective reports capable of being shared. |
| Mooring Equipment Guidelines | OCIMF | Guidelines | First published in 1992 and now on a third edition reflecting on changes in ship and terminal design as the shipping industry has always been concerned with safe mooring practices. A fundamental aspect of this concern entails the development of mooring systems which are adequate for the intended service, with maximum integration of standards across the range of ship types and sizes. |
| Although numerous standards, guidelines and recommendations concerning mooring practices, mooring fittings and mooring equipment exist they are often incomplete. These guidelines are intended to provide an extensive overview of the requirements for safe mooring from both a ship and terminal perspective embrace the full spectrum of issues from the calculation of a ship’s restraint requirements, the selection of rope and fitting types to the retirement criteria for mooring lines. | |||
| Accident prevention – The use of hoses and hard-arms at marine terminals handling Liquefied Gas (2nd edition) | SIGTTO | Industry Guidance | This paper covers accidents relating to hoses, hard-arms and pipeline incidents close to ship or shore manifolds. The report only covers the liquefied gas industry. Where possible, and resulting from incidents, the design and operation of various equipment types is discussed. |
| The selection and testing of valves for LNG applications | SIGTTO | Industry Guidance | This document provides guidance to designers and operators on the general requirements for valves for services, generally designed with an operating temperature range of +80 °C to -196 °C. This guidance is primarily intended for the shipping and storage of these products but may be applied throughout the LNG and LPG industries as appropriate. |
| The selection and testing of valves for LNG applications | SIGTTO | Industry Guidance | This document provides guidance to designers and operators on the general requirements for valves for services, generally designed with an operating temperature range of +80 °C to -196 °C. This guidance is primarily intended for the shipping and storage of these products but may be applied throughout the LNG and LPG industries as appropriate. |
| Guidance for the prevention of rollover in LNG ships | SIGTTO | Information Paper | For receiving terminals, the issues are generally well understood and suitable mitigation methods are in place. For LNG ships, while the circumstances leading to rollover are quite unusual, rollover has occurred, leading to the release of this information paper. |
| SIGTTO – LNG ship to ship transfer guideline | SIGTTO | Industry Guidance | The LNG Ship to Ship Transfer Guidelines, published in 2001, covers the transfer of LNG from LNG carriers at anchor, alongside a shore jetty or while underway. They are also useful for reference when establishing rules and procedures for transfer operations between seagoing ships and LNG regasification vessels (LNGRV) or LNG floating storage and offloading vessels (FSOs) in inshore waters. |
| SIGTTO – Ship/shore interface – Safe working practice for LPG & Liquefied Chemical Gas Cargoes | SIGTTO | Industry Standard | The main objective of this document is to improve safety at the ship/shore interface. The document considers cargo transfer operations and the processes involved within the ship/shore interface to ensure cargo transfer of LPG and liquefied chemical gases is carried out safely and reliable. |
| SIGTTO Crew Safety Standards and Training for large LNG carriers | SIGTTO | Industry Standard | This document has been prepared primarily for the guidance of ship owners and operators who may be entering LNG ship operation for the first time. It is also of use to existing LNG operators who are training new crews due to expansion. |
| The document highlights the salient statutory requirements for the training of LNG tanker crews and the provisions of the International Standards of Training and Watch Keeping Convention, as it applies to gas tankers. It outlines the publications which are recommended for carriage on board all LNG tankers. It also provides advice on the application of the International Safety Management Code to the training and management of tanker crews. In all these matters, it draws heavily on the experience of SIGTTO member companies that have extensive operating experience with this class of vessel. Hence, it may be considered, as a guide to current best industry practice. | |||
| Industry Standards | |||
| Static Electricity (NFPA 77) | NFPA | Best Practices | In addition to being a danger to individuals and an operating problem in industry, static electricity is often the ignition source for an ignitable mixture. The latest, best practices are outlined in this document to help guard against fires and explosions given clear guidelines for the assessment of ignition potential and protocols for fire prevention. |
| NFPA 52 Vehicular Gaseous Fuel Systems Code | NFPA | Standard | Standard with requirements for gaseous fuel systems: |
| CNG and LNG systems on all vehicle types | |||
| Fuel compression, processing, storage, and dispensing systems | |||
| CNG residential fuelling facilities (RFF-CNGs) | |||
| LNG fuelling facilities | |||
| LNG fire protection | |||
| Installation of ASME tanks for LNG | |||
| LNG and CNG on Commercial Marine Vessels and Pleasure Craft | |||
| Classification of Class I/II Hazardous (Classified) Locations for Electrical Installations in Chemical Process Areas (NFPA 497A/B) | NFPA | Standard | This practice applies to those locations where flammable gases or vapours, flammable liquids, or combustible liquids are processed or handled; and where their release into the atmosphere may result in their ignition by electrical systems or equipment. |
| Standard for the production, handling and storage of LNG (NFPA 59A) | NFPA | Standard | Standard that applies to the location, design, construction, maintenance and operation of all facilities that liquefy, store, vaporise and handle natural gas. It also deals with the training of personnel involved with LNG. |
| Protection against ignitions arising out of statics, lightning and stray currents API RP 2003:Ed 7 | API | Information paper | Presents the current state of knowledge and technology in the fields of static electricity, lightning, and stray currents applicable to the prevention of hydrocarbon ignition in the petroleum industry and is based on both scientific research and practical experience. The principles discussed are applicable to other operations where ignitable liquids and gases are handled. |
| API Standard 620 (2002) – Design and construction of Large, Welded, Low-Pressure Storage Tanks | API | Standard | Appendix Q of this standard covers specific requirements for the material, design and fabrication of tanks to be used for the storage of liquefied ethane, ethylene and methane. |
| EEMUA Publication 147 – Recommendations for the design and construction of refrigerated liquefied gas storage tanks | EEMUA | Standard | This publication contains basic recommendations for the design and construction of single, double and full containment tanks for the bulk storage of refrigerated liquefied gases down to -165 °C, for both metal and concrete material/28/. Liquids covered by the scope of this publication, which is intended for international application, include LPG, ethylene, LNG and similar hydrocarbons. |
| ISGOTT – International safety guide for oil tankers & terminals | ICS | Safety Guide | The International Safety Guide for Oil Tankers & Terminals (ISGOTT) is devolved for the safe carriage and handling of crude oil and petroleum products on tankers and at terminals. To ensure that the ISGOTT reflects the current best practice and legislation the guideline is reviewed by the ICS and OCIMF, together with the International Association of Ports and Harbours (IAPH). It is recommended by the industry that a copy of the International Safety Guide for Oil Tankers & Terminals (ISGOTT) is kept and used on board every tanker and in every terminal so that there is a consistent approach to operational procedures and shared responsibilities for operations at the ship/shore interface. |
| OCIMF | |||
| IAPH | |||
| ISGINTT – International safety guide for Inland Navigation Tank-barges and Terminals | CCNR | Safety Guide | The Oil Companies International Marine Forum (OCIMF) together with other stakeholders for inland waterways, like the CCNR developed the International Safety Guide for Inland Tank-barges and Terminals (ISGINTT). The International Safety Guide for Inland Tank-barges and Terminals is not intended to replace or to amend current legislation as ADN and RVIR, but to provide additional recommendations. The CCNR supports the Guide as the principal industry reference manual on the safe operation of tankers and terminals that serve them. |
| OCIMF | The ISGINTT does not give restrictions on fuel properties that can or cannot be used for the propulsion of inland ships. The link with LNG can be found in the hazards that arise for liquids with a flashpoint below 60 °C. The ISGINTT does distinguish between volatile and non-volatile liquids based on their flashpoints. However, this link is purely based on hazard identification and not on shipping fuel related activities. | ||
| Other | |||
| LNG Operating Regulations 1/7/2016 | Port of Gothenburg | Port Regulation | Regulation valid for LNG Bunkering Operations in the Port of Gothenburg. |
| LNG access code for truck loading for the Zeebrugge LNG terminal | Port of Zeebrugge | Port Regulation | This LNG access code for truck loading consists of a standard set of rules and procedures governing regulated access to the LNG services offered at the LNG terminal in Zeebrugge. It contains operating rules for LNG truck loading, an LNG truck approval procedure, LNG specifications and detailed procedures for determining the LNG mass loaded. |
| Study on the completion of an EU framework on LNG – fuelled ships and its relevant fuel provision infrastructure | European Commission | Study Report | Lot 1, out of the 4 Lots comprising the EU Study on the completion of an EU framework on LNG-fuelled ships and its relevant fuel provision infrastructure. |
| The study provides for an analysis of the EU context in LNG bunkering, in particular addressing the Gaps found in the regulatory frame and developing. | |||
| To analyse, further evaluate and propose solutions to the identified gaps and barriers on the basis of the findings of the EMSA study, while taking into account the on-going work and preliminary results at the ISO and the IMO; work and initiatives that have been already undertaken at local and national level; findings from relevant TEN-T projects. | |||
| To identify and address the remaining issues related to the regulatory framework, standardisation of the LNG bunkering process, the permitting process, QRA and incident reporting, proposing solutions for an EU-wide harmonisation. | |||
| PGS 33-2 – Dutch national guideline for LNG bunkering of ships | The Netherlands | National Guidelines | The Dutch national guideline for LNG bunkering of ships is one of the PGS guidelines, which are formulated to provide design requirements for a safe installation. Although PGS 33-2 in itself is no regulation, these guidelines are used by the authorities and industry to prove conformity to the regulation by complying with the requirements of PGS. Authorities can chose to make reference to the guideline and thereby enforce it. |
| PGS 33-2:2014 provides a consistent and transparent framework for shore-to-ship LNG bunker station design. | |||
| The guideline includes harmonised risk analysis procedures for the siting of LNG bunker stations. For a detailed evaluation of technical guidelines and standards including PGS 33-2 reference is made to “Sub-activity report 2.3 II LNG bunkering procedures”. | |||
| Bunkering of Liquefied Natural Gas-Fuelled Marine Vessels in North America | ABS | Study Report | ABS’ report on Bunkering of Liquefied Natural Gas-Fuelled Marine Vessels in North America aims to provide guidance to potential owners and operators of gas-fuelled vessels, as well as LNG bunkering vessels and facilities, to help them obtain regulatory approval for projects. This report lays out an integrated approach to addressing the federal, state, provincial and local requirements that may impact LNG bunkering infrastructure. |
| BS 4089:1999 – Specification for Metallic Hose Assemblies for Liquefied Petroleum Gases and Liquefied Natural Gases | UK National Standards Body (NSB) | British Standard | This British Standard specifies requirements and test methods for metallic hose assemblies used for the loading and unloading of LPG and LNG under pressure. These hoses are primarily used for road and rail tankers or for ship to shore duties. |
| ISO/DTS 16901 | This technical specification, published in March 2015, provides a common approach and guidance to those undertaking assessments of the major safety hazards as part of the planning, designing and operation of LNG facilities onshore and at shoreline using risk based methods and standards, to enable a safe design and operation of LNG facilities. | ||
| Guidance on performing risk assessment in the design of onshore LNG installations including the Ship/Shore interface | The technical specification is aimed to be applied both to export and import terminals but can be applicable to other facilities such as satellite and peak shaving plants. | ||








