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PD ISO/TS 16901:2015

Superseded
Superseded

A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.

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superseded

A superseded Standard is one, which is fully replaced by another Standard, which is a new edition of the same Standard.

Guidance on performing risk assessment in the design of onshore LNG installations including the ship/shore interface
Available format(s)

Hardcopy , PDF

Superseded date

26-04-2023

Language(s)

English

Published date

31-03-2015

This Technical Specification provides a common approach and guidance to those undertaking assessment of the major safety hazards as part of the planning, design, 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. The environmental risks associated with an LNG release are not addressed in this Technical Specification.

This 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.

It applies to all facilities inside the perimeter of the terminal and all hazardous materials including LNG and associated products: LPG, pressurised natural gas, odorizers, and other flammable or hazardous products handled within the terminal.

The navigation risks and LNG tanker intrinsic operation risks are recognised, but they are not in the scope of this Technical Specification. Hazards arising from interfaces between port and facility and ship are addressed and requirements are normally given by port authorities. It is assumed that LNG carriers are designed according to the IGC code, and LNG fuelled vessels receiving bunker is designed according to IMO’s regulations.

Border between port operation and LNG facility is when the ship/shore link (SSL) is established.

It is not intended to specify acceptable levels of risk; however, examples of tolerable levels of risk are referenced.

This Technical Specification is not intended to be used retrospectively.

It is recognised that national and/or local laws, regulations, and guidelines take precedence where they are in conflict with this Technical Specification.

Reference is made to ISO31010 and ISO17776 with regard to general risk assessment methods, while this Technical Specification focuses on the specific needs scenarios and practices within the LNG industry.

Committee
PSE/17
DocumentType
Standard
Pages
68
PublisherName
British Standards Institution
Status
Superseded
SupersededBy

Standards Relationship
ISO/TS 16901:2015 Identical

IEC/ISO 31010:2009 Risk management - Risk assessment techniques
ISO 31000:2009 Risk management Principles and guidelines
IMO I104 : 1993 SUPP 2013 INTERNATIONAL CODE FOR THE CONSTRUCTION AND EQUIPMENT OF SHIPS CARRYING LIQUEFIED GASES IN BULK (IGC CODE)
ISO 17776:2016 Petroleum and natural gas industries Offshore production installations Major accident hazard management during the design of new installations
NORSOK S 001 : REV 4 TECHNICAL SAFETY
EN 1473:2016 Installation and equipment for liquefied natural gas - Design of onshore installations
ISO 28460:2010 Petroleum and natural gas industries Installation and equipment for liquefied natural gas Ship-to-shore interface and port operations
ISO/IEC Guide 73:2002 Risk management Vocabulary Guidelines for use in standards
NFPA 59A : 2016 PRODUCTION, STORAGE, AND HANDLING OF LIQUEFIED NATURAL GAS (LNG)
EN 1160 : 1996 INSTALLATIONS AND EQUIPMENT FOR LIQUEFIED NATURAL GAS - GENERAL CHARACTERISTICS OF LIQUEFIED NATURAL GAS
EN 16348:2013 Gas infrastructure - Safety Management System (SMS) for gas transmission infrastructure and Pipeline Integrity Management System (PIMS) for gas transmission pipelines - Functional requirements

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£260.00
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