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Installation and equipment for
liquefied natural gas Ð
Ship to shore interface
The European Standard EN 1532 : 1997 has the status of a
British Standard
ICS 75.200
NO COPYING WITHOUT BSI PERMISSION EXCEPT AS PERMITTED BY COPYRIGHT LAW
Copyright British Standards Institution
Provided by IHS Markit under license with BSI - Uncontrolled Copy
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BS EN
1532 : 1997
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BRITISH STANDARD
BS EN 1532 : 1997
Committees responsible for this
British Standard
The preparation of this British Standard was entrusted to Technical Committee
GSE/38, Installation and equipment for LNG, upon which the following bodies were
represented:
British Gas plc
Department of Transport
Health and Safety Executive
Institution of Gas Engineers
This British Standard, having
been prepared under the
direction of the Engineering
Sector Board, was published
under the authority of the
Standards Board and comes into
effect on
15 August 1997
 BSI 1997
Amendments issued since publication
Amd. No.
Date
Text affected
The following BSI references
relate to the work on this
standard:
Committee reference GSE/38
Draft for comment 94/711296 DC
ISBN 0 580 27953 7
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BS EN 1532 : 1997
Contents
Page
Inside front cover
ii
2
3
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Committees responsible
National foreword
Foreword
Text of EN 1532
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i
BS EN 1532 : 1997
National foreword
This British Standard has been prepared by Technical Committee GSE/38, and is the
English language version of EN 1532 : 1996 Installation and equipment for liquefied
natural gas Ð Ship to shore interface, published by the European Committee for
Standardization (CEN).
Cross-references
Publication referred to
Corresponding British Standard
EN 1160 : 1996
BS EN 1160 : 1997 Installations and equipment for liquefied
natural gas Ð General characteristics of liquefied natural
gas
BS EN 50014 : 1993 Electrical apparatus for potentially
explosive atmospheres Ð General requirements
BS EN 50015 : 1994 Electrical apparatus for potentially
explosive atmospheres Ð Oil immersion `o'
BS EN 50016 : 1996 Electrical apparatus for potentially
explosive atmospheres Ð Pressurized apparatus `p'
BS EN 50017 : 1994 Electrical apparatus for potentially
explosive atmospheres Ð Powder filling `q'
BS EN 50018 : 1995 Electrical apparatus for potentially
explosive atmospheres Ð Flameproof enclosures `d'
BS EN 50019 : 1994 Electrical apparatus for potentially
explosive atmospheres Ð Increased safety `e'
BS EN 50020 : 1995 Electrical apparatus for potentially
explosive atmospheres Ð Instrinsic safety `i'
BS 5501 Electrical apparatus for potentially explosive
atmospheres
BS 5501 : Part 8 : 1988 Encapsulation `m'
BS 5501 : Part 9 : 1982 Specification for intrinsically safe
electrical systems `I'
BS EN 50054 : 1991 Electrical apparatus for the detection
and measurement of combustible gases Ð General
requirements and test methods
BS EN 50056 : 1991 Specification for electrical apparatus for
the detection and measurement of combustible gases Ð
Performance requirements for Group I apparatus indicating
up to 100 % (V/V) methane
BS EN 50057 : 1991 Electrical apparatus for the detection
and measurement of combustible gases Ð Performance
requirements for Group II apparatus indicating up to 100 %
lower explosive limit
BS EN 50058 : 1991 Specification for electrical apparatus for
the detection and measurement of combustible gases Ð
Performance requirements for Group II apparatus
indicating up to 100 % (V/V) gas
EN 50014 : 1992
EN 50015 : 1994
EN 50016 : 1995
EN 50017 : 1994
EN 50018 : 1994
EN 50019 : 1994
EN 50020 : 1993
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EN 50028
EN 50039 : 1980
EN 50054 : 1991
EN 50056 : 1991
EN 50057 : 1991
EN 50058 : 1991
Compliance with a British Standard does not of itself confer immunity
from legal obligations.
Summary of pages
This document comprises a front cover, an inside front cover, pages i and ii, the
EN title page, pages 2 to 14, an inside back cover and a back cover.
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 BSI 1997
EN 1532
EUROPEAN STANDARD
NORME EUROPEÂENNE
EUROPAÈISCHE NORM
March 1997
ICS 75.200
Descriptors: Gas installation, liquefied natural gas, earth stations, ships, interfaces, transfer, junctions, safety, accident prevention, haz ards,
hazardous areas, fire protection, stopping devices, mooring devices, design
English version
Installation and equipment for liquefied natural gas Ð
Ship to shore interface
Installations et eÂquipements relatifs au gaz naturel
liqueÂfie РInterface terre navire
Anlagen und AusruÈstung fuÈr FluÈssigerdgas Ð
Schnittstelle zwischen Schiff und Land
This European Standard was approved by CEN on 1997-02-24. CEN members are
bound to comply with the CEN/CENELEC Internal Regulations which stipulate the
conditions for giving this European Standard the status of a national standard
without any alteration.
Up-to-date lists and bibliographical references concerning such national standards
may be obtained on application to the Central Secretariat or to any CEN member.
The European Standards exist in three official versions (English, French, German).
A version in any other language made by translation under the responsibility of a
CEN member into its own language and notified to the CEN Central Secretariat has
the same status as the official versions.
CEN members are the national standards bodies of Austria, Belgium, Denmark,
Finland, France, Germany, Greece, Iceland, Ireland, Italy, Luxembourg, Netherlands,
Norway, Portugal, Spain, Sweden, Switzerland and United Kingdom.
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CEN
European Committee for Standardization
Comite EuropeÂen de Normalisation
EuropaÈisches Komitee fuÈr Normung
Central Secretariat: rue de Stassart 36, B-1050 Brussels
 1997 Copyright reserved to CEN members
Ref. No. EN 1532 : 1997 E
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Page 2
EN 1532 : 1997
Foreword
Page
This European Standard has been prepared by
Technical Committee CEN/TC 282, Installation and
equipment for LNG, the secretariat of which is held
by AFNOR.
This European Standard shall be given the status of a
national standard, either by publication of an identical
text or by endorsement, at the latest by
September 1997, and conflicting national standards
shall be withdrawn at the latest by September 1997.
According to the CEN/CENELEC Internal Regulations,
the national standards organizations of the following
countries are bound to implement this European
Standard: Austria, Belgium, Denmark, Finland, France,
Germany, Greece, Iceland, Ireland, Italy, Luxembourg,
Netherlands, Norway, Portugal, Spain, Sweden,
Switzerland and the United Kingdom.
Contents
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Foreword
0
Introduction
1
Scope
2
Normative references
3
Definitions and abbreviations
3.1 Definitions
3.2 Abbreviations
4
List of items that make up the ship to
shore interface
5
Description of LNG and associated
hazards
5.1 Description of LNG
5.2 Hazards associated with LNG
5.3 Hazards associated with LNG transfer
5.4 Potential external factors
6
Hazardous areas
7
Safety precautions
7.1 General
7.2 Basic precautions
7.3 Additional precautions
8
Ship equipment
8.1 Ship's mooring equipment
8.2 Ship's working platform and cargo
manifold arrangements
8.3 Motor operated valves (MOV) for ESD
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8.4
Ship's cargo control room operating
devices
8.5 Ship's firefighting equipment
8.6 Protection of the ship's structure
8.7 Communication equipment
8.8 Ship's electrical safety
8.9 LNG pumping system
8.10 Cooling down systems
8.11 Bunkering connection
8.12 Fresh water connection
8.13 Arrangements for personnel access
9
Ship/shore transfer facility equipment
9.1 General
9.2 Design and construction of the jetty
and associated equipment
9.3 Loading/unloading arms
9.4 Communication equipment (see 8.7)
9.5 Firefighting equipment and procedures
9.6 Main control room
9.7 Vapour return system
9.8 Crew and personnel access (see 7.2.9)
9.9 Motor operated valves, (MOV) for ESD
9.10 Jetty's electrical safety
9.11 Ship's storing arrangements
10
LNG transfer procedure
10.1 Necessary provisions prior to ship
acceptance
10.2 Conditions for port entry
10.3 Conditions to be fulfilled prior to
connecting loading/unloading arms
10.4 Conditions to be fulfilled prior to the
transfer of LNG
10.5 Fulfilment of the safety conditions
during transfer operations
10.6 Conditions to be fulfilled following
ship's transfer
10.7 Shore and ship protection of
personnel on duty
10.8 Responsibilities
11
Training of personnel
Annex A (informative) General safety
philosophy
Annex B (informative) Bibliography
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 BSI 1997
Page 3
EN 1532 : 1997
EN 50016
Each LNG port facility and terminal should have its
own specific safety systems determined by Hazard
Analysis and LNG carriers using the facility should be
compatible with these systems. In general, for all
vessels, particular care should be taken to ensure that
the basic requirements laid down in this standard are
understood and applied at each cargo transfer.
In order to define the arrangement which will ensure
the best possible conditions for ship to shore transfer,
in particular regarding safety, it is necessary to set up
this standard which, as far as possible, will lead to the
harmonization of the differing requirements of the ship
and the terminal.
This standard governs the ship/shore interface taking
into account the publications of the Society of
International Gas Tankers and Terminal Operators
(SIGTTO), Oil Companies International Marine Forum
(OCIMF) and the International Maritime Organization
(IMO). In particular, this applies in matters pertaining
to safety.
1 Scope
EN 50017
EN 50018
EN 50019
EN 50020
EN 50028
EN 50039
EN 50054
This European Standard gives recommendations and
requirements for the terminal and on board the ship to
ensure the safe transfer of LNG at receiving and
exporting terminals.
It is applicable to the ship/shore LNG transfer systems
including:
± ship to shore connections;
± all safety aspects of transfer operations;
± any other operations that occur while the ship is
moored on the jetty.
EN 50056
EN 50057
2 Normative references
This European Standard incorporates by dated or
undated reference, provisions from other publications.
These normative references are cited at the
appropriate places in the text and the publications are
listed hereafter. For dated references, subsequent
amendments to or revisions of any of these
publications apply to this European Standard only
when incorporated in it by amendment or revision. For
undated references the latest edition of the publication
referred to applies.
EN 1160
EN 50014
EN 50015
Installation and equipment for
liquefied natural gas Ð General
characteristics of liquefied natural gas
Electrical apparatus for potentially
explosive atmospheres Ð General
requirements
Electrical apparatus for potentially
explosive atmospheres Ð Oil
immersion `o'
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 BSI 1997
EN 50058
prEN 1127-1
prEN 1473
prEN 1474
prEN 50145
ISO 10497
Electrical apparatus for potentially
explosive atmospheres Ð Pressurized
apparatus `p'
Electrical apparatus for potentially
explosive atmospheres Ð Powder
filling `q'
Electrical apparatus for potentially
explosive atmospheres Ð Flameproof
enclosure `d'
Electrical apparatus for potentially
explosive atmospheres Ð Increased
safety `e'
Electrical apparatus for potentially
explosive atmospheres Ð Intrinsic
safety `i'
Electrical apparatus for potentially
explosive atmospheres Ð
Encapsulation `m'
Electrical apparatus for potentially
explosive atmospheres Ð Intrinsically
safe electrical systems `i'
Electrical apparatus for the detection
and measurement of combustible
gases Ð General requirements and test
methods
Electrical apparatus for the detection
and measurement of combustible
gases Ð Performance requirements for
Group 1 apparatus indicating up
to 100 % (v/v) methane
Electrical apparatus for the detection
and measurement of combustible
gases Ð Performance requirements for
Group II apparatus indicating up
to 100 % lower explosive limit
Electrical apparatus for the detection
and measurement of combustible
gases Ð Performance requirement for
Group II apparatus indicating up
to 100 % (v/v) gas
Safety of machinery Ð Fire and
explosions Ð Part 1: Explosion
prevention and protection
Installation and equipment for
liquefied natural gas Ð Design of
onshore installation
Installation and equipment for
liquefied natural gas Ð Design and
testing of loading/unloading arms
Electrical apparatus for potentially
explosive gas atmospheres Ð
Classification of hazardous areas
Testing of valves Ð Fire type-setting
requirements
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0 Introduction
Page 4
EN 1532 : 1997
3 Definitions and abbreviations
For the purposes of this European Standard the
definitions of prEN 1474 and the following definitions
apply.
3.1 Definitions
3.1.1 ship/shore transfer facilities
A jetty including all the ship/shore interface equipment
for receiving or exporting LNG.
3.1.2 communication
All methods of transmitting written or oral information.
It also includes information covered by data links.
3.1.3 interface
All the operations of the ship and shore relating to
LNG cargo transfer, ship's access or ship's supplies.
3.1.4 main control room
A control room situated in the terminal from which
central control is directed.
3.1.5 jetty control centre
A control centre situated on or adjacent to the jetty
primarily to control the loading/unloading arms.
3.1.6 ship cargo control room
A control room situated on board the ship from which
the control of the ship's transfer operation is directed.
3.1.7 emergency shut down (ESD)
A method that safely and effectively stops the transfer
of LNG between ship and shore or vice versa.
3.1.8 emergency release system (ERS)
A system that provides a positive means of quick
release of loading/unloading arms and safe isolation
between ship and shore.
3.1.9 emergency release procedure (ERP)
A procedure that is intended to provide a positive
means of quick release and safe isolation between ship
and shore.
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3.1.10 ship's cargo manifold
The flanged pipe assembly, mounted on board ship to
which the outboard flange of the loading/unloading
arms are connected.
3.1.11 terminal
An LNG plant with loading/unloading facilities.
3.1.12 transfer
Loading or unloading operation.
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3.2 Abbreviations
For the purpose of this European Standard, the
following abbreviations apply.
± LNG: Liquefied natural gas;
± NG: Natural gas;
± MOV: Motor operated valve.
4 List of items that make up the ship to
shore interface
The items to be especially considered for LNG transfer
are:
± the ship's safe mooring at the jetty;
± gangway access from jetty to ship;
± all the communications between ship and shore;
± all instrument and electrical connections used
across the interface;
± loading/unloading;
± bunkering from the terminal or by supply barge;
± liquid nitrogen connection;
± ship's storing.
5 Description of LNG and associated
hazards
5.1 Description of LNG
The characteristics of LNG are described in EN 1160.
5.2 Hazards associated with LNG
The main hazards are defined in EN 1160 and those
most important in the transfer of LNG are:
± the cryogenic effects resulting from the very low
temperatures. These low temperatures can cause
injury to people (frost bite), and also cause damage
to non-cryogenic materials, which lose their
mechanical properties, become brittle and fracture;
± the potential hazards of fire or explosion from
leaks or spillage of LNG;
± the overpressure caused by rapid phase transition
(RPT), due to the interaction between LNG and
water;
± overpressure due to thermal expansion of trapped
LNG.
5.3 Hazards associated with LNG transfer
The main hazards are associated with:
± cooldown, warmup, purging and draining of
loading/unloading arms;
± overflows of storage tanks (ship and shore);
± overpressure of storage tanks (ship and shore).
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Page 5
EN 1532 : 1997
5.4 Potential external factors
The external hazards that should be considered in the
transfer operations are:
1) natural environment:
± atmospheric conditions (wind, lightning, etc.);
± sea conditions;
± seismic conditions;
± rise and fall of the tide.
2) other hazards:
± jetty contact;
± collision with another ship or the jetty;
± mooring lines breaking;
± fire at the terminal or its surroundings;
± LNG ship movement generated by the suction
effects from ships passing nearby.
6 Hazardous areas
7.1 General
Safety precautions may differ from location to location
due to local conditions, therefore a hazard analysis
shall be carried out in each case to establish the
minimum safety precautions. The hazard analysis shall
be performed according to prEN 1473. The basic
precautions as outlined in this European Standard are
considered to be the minimum safety precautions
required. The additional precautions, resulting from the
hazard analysis for each terminal shall be considered
as extra to the basic precaution. The terminal and the
ship shall always ensure that this minimum safety level
is maintained by the use of the Ship/Shore Safety
Check List. (In this regard, reference should be made
to the SIGTTO guidelines: Annex B: Reference 6).
7.2 Basic precautions
7.2.1 Restricted harbour areas
In order to guard against unexpected collisions to the
LNG carrier when alongside, restricted areas around
the berth for other maritime traffic should be defined
by the appropriate authorities and the terminal.
7.2.2 Restricted area on the jetty
Areas in which the access of non authorized personnel
is limited should be regulated by the safety rules of the
terminal. These areas correspond, at least in part, to
the area affected by LNG transfer and should be
clearly indicated.
7.2.3 Restricted area on the ship
Areas in which access of non authorized personnel is
limited should be regulated by the safety rules of the
ship. These areas correspond, at least in part, to the
area affected by LNG transfer.
7.2.4 Ship/shore safety check list
The Ship/Shore Safety Check List should be officially
completed by ship and shore personnel before the start
of LNG transfer. (In this regard, reference should be
made to the SIGTTO guidelines: Annex B: Reference 6.)
7.2.5 Mooring arrangements
The ship shall be safely moored in accordance with the
regulations of the local appropriate authority and the
terminal. (In this regard, reference should be made to
the OCIMF guidelines: Annex B: Reference 2.)
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When the ship is moored at the jetty, the ship's gas
dangerous space or zone is added to the jetty's
hazardous area.
(For definition of the ship's gas dangerous space or
zone, reference should be made to the IMO code:
Annex B: Reference 7.)
The hazardous area on the terminal and jetty is
classified in two types:
a) zone 1, for areas where the risk of an explosive
atmosphere exists during normal operation;
b) zone 2, for areas where an explosive atmosphere
could occur in the event of deviation from normal
operation.
For definition of these hazardous areas, reference shall
be made to prEN 1127-1 and prEN 50145.
Within the jetty area, the electrical equipment shall be
set out in accordance with EN 50014 to EN 50020,
EN 50028, EN 50039, EN 50054, EN 50056 to EN 50058
taking into account the zone where it is used and for
non electrical equipment in accordance with
prEN 1127-1. The electrical equipment on the ship
should be in accordance with the relevant Gas Code as
published by IMO.
7 Safety precautions
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Page 6
EN 1532 : 1997
7.2.6 Weather forecast
Weather forecasts shall be available to the ship and
shore at intervals not exceeding 12 h.
7.2.7 Principal sources of ignition
Any risk of sparking in hazardous areas shall be
avoided.
The choice of which protection measures to use in
order to avoid ignition caused by electrical and non
electrical equipment is to be made according to the
existing local standards and according to the nature of
the hazardous area.
There is a possible risk of sparking due to the
difference in electrical potential between the ship and
the jetty, when the loading/unloading arms are being
connected or disconnected.
Arrangements should be taken to avoid the risk of
sparking from this source through the installation of an
insulation flange between ship and shore.
7.2.8 Data transfer and communication
A means of transferring data shall be provided
between ship and shore. When the ship is moored at
the jetty, ESD information shall be transmitted by a
hard-wire data link.
An oral communication system such as hand held
radios shall be provided. It should have a separate
back up system which may be a land line telephone.
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7.2.9 Access
A minimum of two access ways between the ship and
the jetty should be provided:
± one access, provided for personnel and crew, shall
be used for escape in the event of an emergency. It
shall be located near to the ship's accommodation
area;
± the second access, provided for operating
personnel, should be located away from the
immediate vicinity of the manifold area.
7.2.10 Fire and leak detection
Leak and fire detection sensors should be installed in
all hazardous areas as per recommendations in
prEN 1473 and shall be operational at all times. The
ESD resulting from fire and/or leak detection should
be transferred to the ship as given in 7.2.8. The ESD
shall be initiated as given in prEN 1473.
7.2.11 Fire protection
Measures shall be provided to protect personnel and
essential equipment from a fire, both on shore and on
board ship, so that the risk of escalation of an incident
is minimized.
7.2.12 Fire fighting
There are four specific reasons for providing fire
fighting equipment:
a) to extinguish a small fire;
b) to safeguard people affected by a larger fire;
c) to control a fire and to prevent it from spreading,
pending the arrival of the Fire Authority;
d) to protect the means of access for the Fire and
Emergency Services.
The extent of the fire fighting equipment supplied will
depend on a variety of factors and should be the
subject of a hazard assessment by the terminal.
The following items should be considered:
e) the causes and types of fire that might be
encountered;
f) the escape routes for ship and shore personnel;
g) the size, nature and frequency of ships using the
terminal;
h) the size of the berths and of the ships and their
distance from other industrial hazards and
population centres;
i) the provision of `off site' fire fighting services
including fire boats;
j) the time needed to mobilize the Fire Authority;
k) the emergency preparation and planning
procedures.
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The mooring arrangements should suit the terminal
facility. As a minimum, the following points shall be
taken into account:
± current;
± wind;
± surge due to passing ships;
± height of tides;
± waves and swell;
± change of freeboard;
± variety of ships received.
The winches or capstans on the jetty area shall be
suitable for operation according to the hazardous area
classification in which they are located.
The fenders shall be located so as to contact the hull
at the frame areas on the parallel body. The fenders
should leave sufficient surface area to avoid damaging
the ship's hull. They shall not obscure the inlets and
outlets of the ship's circulation or ballast sea water.
The ship should be moored safely and in a manner
which enables departure in the shortest possible time.
The berth area shall be maintained at a suitable depth,
to ensure sufficient underkeel clearance at all states of
the tide.
Page 7
EN 1532 : 1997
Permanently installed equipment for fire fighting and
control should be kept ready for instant use while the
ship is alongside. This equipment should be as
described in prEN 1473.
Portable or trailer mounted units should also be
provided but only used as a backup to the permanent
installation and for dealing with small fires.
A plan showing the location and type of all fire fighting
equipment on or adjacent to the jetty should be
permanently displayed at the berth, along with any
necessary instructions and fire procedures. A safety
plan should be available onboard the ship, in
accordance with applicable IMO conventions.
7.2.13 Protection from leakage and spillage of
LNG
Means of protection shall be provided both on the ship
and on shore to minimize the consequences of spillage
and leakage of LNG. A procedure shall be agreed both
on ship and on shore to minimize any damage
resulting from spillage, bearing in mind the effect LNG
has on non cryogenic steels, i.e. brittle fracture. Means
of protecting the deck of the ship in the manifold area
should be provided together with means of diverting
any spillage overboard.
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7.2.14 General safety philosophy and procedures
for stopping ship/shore transfer
7.2.14.1 General
The methods of isolation and disconnection are
described below and are further defined by a flow
diagram in annex A.
7.2.14.2 Standard procedure of disconnection
Except in cases of emergency, standard operating
procedures shall be used to stop the transfer of LNG.
The design of the pipework and loading/unloading
arms shall allow for the safe stoppage of LNG transfer
and the return of all the arms to the normal empty
position in the shortest possible time. The design shall
also consider the effect of ice formation on the arms,
where necessary.
During LNG transfer the number of non-LNG
connections between ship and shore shall be restricted
to the minimum to minimize the time of disconnection.
By way of guidance, the normal disconnecting
operation should be completed in about 1 h.
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7.2.14.3 Emergency shut down (ESD)
A means of Emergency Shut Down (ESD), which is
acceptable to the terminal operator, shall be
operational before LNG transfer is commenced. ESD
directly affects the procedures used in the transfer of
LNG, as follows:
a) the function of the ESD is mainly:
± to stop the ship's gas compressors and the
terminal's pumps if the ship is being loaded;
± to stop the ship's pumps and terminal's gas
compressors if the ship is being unloaded;
± to close the ship's ESD valves on the manifold;
± to close the shore ESD valves. Allowances shall
be made to avoid surge pressures developing
during this operation;
± to drain the arms, if operationally required;
b) the ESD should be arranged so as to be manually
operated from a number of control points;
c) the events that should automatically initiate the
ESD are:
± fire detection;
± detection of the first threshold of drift (abnormal
displacement of the ship);
± high level in ship or shore storage tanks;
± detection of liquid spills;
± high and low pressure or vacuum in ship or
shore storage tanks;
± loss of electric or control power on ship or
shore;
d) the indication of an ESD is sent to the main
control room, the ship's cargo control room and the
jetty control centre.
The ESD can also be initiated manually from each of
these control rooms and will always automatically
initiate all the ESD functions. Transmission of the
alarm shall be by an effective two-way data transfer
link, one for sending the alarm and another for
returning the ESD command.
ESD systems shall be designed to operate during a fire
at a temperature ranging from 1100 ÊC to 350 ÊC for a
period of 1,5 to 10 min respectively.
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7.2.14.4 Emergency release procedure after
completion of ESD (ERP1)
An emergency disconnection is carried out only when
normal disconnection cannot be achieved.
If following the operation of an ESD, an emergency
condition still exists, the arms should be disconnected
using the emergency release system (ERS).
The ERS is either automatically activated by the range
monitoring system or manually operated from the jetty
control panel, the main control room or the ship's
cargo control room.
The disconnection of the ERS may be hazardous in the
event of untimely operation, therefore provisions shall
be taken to prevent false operation.
Two disconnecting conditions need to be considered:
± disconnection after draining of the arms; in this
case, the arm is disconnected in the empty condition
(emergency empty unbalanced condition, see
annex A);
± disconnection before draining of the arms; in this
case, the arm is disconnected in the full condition
(emergency full unbalanced condition, annex A);
± physical disconnection shall not be activated until
the two ball valves in the ERC assembly are proved
closed. (In this regard, reference should be made to
prEN 1474.)
7.2.14.5 Emergency release procedure before ESD
initiation and completion (ERP2)
In order to achieve the maximum protection for the
terminal, in the case of excessive drift of the ship or
for other reasons, the emergency release procedure
can be initiated before completion of the ESD cycle.
Initiation is automatically set by the range monitoring
system or manually operated from the jetty control
panel or the main control room.
Immediate release of the arms shall be followed by
raising the arms into the stored position to avoid the
risk of colliding with the ship's structure when it leaves
the berth.
The departure of the ship can only proceed in safe
conditions and with the authority of the ship's master.
7.2.15 Material of construction
All the ship and shore piping equipment in contact
with LNG shall be made of suitable material, as
described in EN 1160.
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7.2.16 LNG loading/unloading arms
Only rigid articulated piping shall be used for LNG
transfer operations between ship and shore as defined
in prEN 1474.
7.3 Additional precautions
Additional precautions may be required as identified by
the Hazard Analysis carried out by the terminal.
To allow for the quick departure of the ship in the
safest possible way, all the ship/shore connections
should be equipped with a quick release system.
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Consideration should be given to the following items:
± quick release of the mooring system (only on
shore);
± quick retraction gangway;
± quick disconnection of electric cables;
± quick release of all other ship/shore connections.
The ERS valves may be closed in the ESD sequence to
allow for an emergency release if this is required.
NOTE. The purpose of the additional precautions is, among other
things, to enable the ship to be released from all of her
connections with the terminal within the shortest possible time
without any increased risk. The release of the ship can only be
achieved with the full knowledge and agreement of the ship's
master.
8 Ship equipment
8.1 Ship's mooring equipment
The ship may be moored using either steel wire ropes
provided with synthetic tails or by ropes made from
synthetic material. It is usually found that nylon tails of
about 11 m are satisfactory for this purpose.
The terminal may be equipped with systems allowing
the continuous verification of the mooring tensions.
This information may be monitored by the terminal
and fed back to the ship.
A towing-off wire should be rigged by the ship at both
bow and stern with the eye of the wire rope
maintained just above sea level to facilitate easy
connection by tugs in the event of an emergency.
8.2 Ship's working platform and cargo manifold
arrangements
Careful consideration should be given to the position
of the ship in the berth and its position relative to the
manifold. In this respect, the management of the
mooring arrangements is of utmost importance.
The ship's manifold should be specified in accordance
with OCIMF recommendations.
The ship's manifold support shall be designed to
withstand the induced loads. These may be due to the
LNG in the transfer arms, possible ice formulation,
wind effect on the arms, and ship's drift and yaw.
The ship shall be equipped with flanges suitable for
connection with the shore arms transfer. The arms
shall be mechanically connected to the ship as
described in prEN 1474.
8.3 Motor operated valves (MOV) for ESD
Emergency shut down valves at each manifold, both
liquid and gas, shall be capable of both local and
remote operation. The valves shall be fire-safe type in
accordance with ISO 10497.
At the design stage, consideration shall be given to the
control of pressure surges. Furthermore, prior to
loading and unloading operations, closing times of the
emergency shutdown valves shall be checked.
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8.4 Ship's cargo control room operating devices
The ship's cargo control room should contain the
following primary equipment:
± VHF communications with the port authority;
± communications systems for the cargo transfer
operation;
± general tank information, such as temperature and
pressure;
± tank level monitoring equipment;
± ESD control devices;
± boil-off gas compressor controls;
± pump controls;
± cargo transfer valve controls;
± trim monitor;
± ballasting control;
± gas monitoring system;
± fire alarm monitoring system.
In addition, operating procedures, safety advice and
emergency procedures relevant to the particular
terminal should be available for the loading/unloading
operations.
8.5 Ship's fire fighting equipment
The fire fighting equipment near the manifold shall
consist of the following:
± dry powder;
± water sprinkler/water curtains;
± water hoses;
± protective clothing.
The manifold area is protected by ship and shore fire
fighting equipment. The ship's fire fighting equipment
shall be independent of the shore facility.
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8.6 Protection of the ship's structure
Protection against the risks of LNG spillages shall be
provided for the deck and the side of the ship in the
manifold area during transfer. The ship shall be
equipped with a drip protection (e.g. tray) under the
manifold to protect the deck. A water curtain or other
suitable means shall be used to protect the side of the
ship.
8.7 Communication equipment
8.7.1 General
All communication equipment for use in hazardous
areas shall be suitable for such use. Facilities shall be
provided for oral communication and data exchange.
8.7.2 Oral
The systems that are normally used for oral
communication are portable radios and telephones
(see 7.2.8). A VHF radio should be available for
communication with the Port Authority.
 BSI 1997
8.9 LNG pumping system
All of the ship's pumps may deliver simultaneously;
however the ship shall only pump at a rate acceptable
to the terminal. Criteria to be considered for the
transfer include:
± the characteristics of the pump or pumps (flow
versus head). These characteristics should be
carefully chosen in both the loading and unloading
operation;
± the temperature of the LNG;
± the cargo flow velocity.
LNG transfer shall be carried out in accordance with
procedures agreed between the ship and the terminal.
The ship's cargo pumps shall have remote start/stop
buttons. Discharge pressure and motor current
information shall be monitored in the ship's cargo
control room.
In the case of a failure of a main cargo pump in a
ship's tank, emergency means of transfer shall be
provided.
8.10 Cooling down systems
When a ship is to be loaded, cooling down of the
ship's equipment should normally be carried out early
enough to prevent delay of loading or unloading.
8.11 Bunkering connection
The bunkering connection on board ship should be
positioned and fitted with reference to OCIMF
procedures. (In this respect, reference should be made
to the OCIMF recommendations: Annex B:
Reference 3.)
8.12 Fresh water connection
Ships should be equipped with standardized flanges as
given in ISO 5620-1 and ISO 5620-2.
8.13 Arrangements for personnel access
For personnel movement and ship's provisioning,
see 7.2.9.
9 Ship/shore transfer facility equipment
9.1 General
The transfer facility shall comply with the minimum
safety requirement as established by the Hazard
Analysis on each LNG terminal.
9.2 Design and construction of the jetty and
associated equipment
8.7.3 Data links
In order for the ship to exchange data with the
terminal via the data link, the ship shall be fitted with
a suitable socket to connect to the terminal
connection. (See 7.2.8.)
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8.8 Ship's electrical safety
As appropriate, electrical instrumentation should be
explosion-proof, intrinsically safe or a certified safe
type in accordance with the relevant marine standard.
9.2.1 General
The design and construction of the jetty shall take into
consideration, where appropriate, the design of all the
ships designated to call at the terminal, and also the
applicable environmental conditions.
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The position of the jetty shall take account of:
± the prevailing winds and currents to limit their
effects on the ship;
± the possibility of collision from passing shipping.
The berth should be located outside main navigation
channels;
± an allowance for the ship to leave the jetty without
outside help;
± the requirements for a suitable turning circle.
The design of the jetty shall take into account:
± design and testing required by civil engineering
works;
± nature of the ground and subsoil;
± the dimensions of the ships to be received;
± cathodic protection, if necessary, of the metallic
parts in contact with water, e.g. the metal pile;
± the need for a jetty containment area to be
installed around the transfer arms, pipelines and
associated valves;
± local requirements;
± applicable loads, including:
± loading/unloading arms;
± piping;
± drainage and surge drums;
± safety equipment;
± any buildings or structures;
± crane and gangway;
± mooring systems;
± stresses brought about by the impact of ships
when berthing;
± maintenance of emergency equipment, e.g.
cranes for overhauling the loading/unloading arms;
± seismic stresses.
9.2.2 Mooring and fendering arrangements
The terminal's mooring system shall be designed and
laid out to allow for the safe handling of the range of
ships to be accommodated at the terminal.
Mooring hooks shall be installed on swivelling and
rotating supports and be fitted with a quick release
mechanism. The quick release can only be operated by
the terminal on the master's authority.
A mooring tension monitoring system may be provided
to enable tensions to be measured and displayed both
on the ship and on the jetty. Load cells to measure the
tension in each mooring wire should be fitted to each
mooring hook and these data should be processed by a
central computer located on the jetty or ashore with a
remote readout available on board the ship.
To allow safe connection of the LNG loading/unloading
arms, the ship's manifold shall be properly positioned
with respect to the loading/unloading arms to be used.
The fenders shall be designed to spread the load of the
berthing impacts over a suitably large area of the ship's
hull.
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9.2.3 Installation of loading/unloading arms
See prEN 1474.
9.2.4 Jetty control centre
It is recommended that the jetty control centre
contains the following equipment:
± the communications system between the main
control room of the terminal and the ship's cargo
control room;
± the loading/unloading arm controls;
± the purging control system for the
loading/unloading arms;
± the emergency uncoupling controls (push button
for ESD and ERS);
± the controls for cooling down the arms;
± the fire fighting control centre (jetty head only);
± weather data station;
± mooring tension monitoring equipment.
For safety reasons, the ship should be constantly
monitored from the jetty control centre.
9.2.5 Jetty piping arrangement
The design of piping and pipe insulation is dealt with
in prEN 1473.
9.3 Loading/unloading arms
The design and testing of the loading/unloading arms is
set out in prEN 1474.
The arms shall be equipped with range monitoring
sensors for measuring displacement in the ship's
position. This information is used by the ESD system.
After draining, a positive nitrogen pressure shall be
used to inactivate the arms before disconnection and
returning them in the stored position.
9.4 Communication equipment (see 8.7)
9.4.1 Oral
Portable radios are the most usual means of oral
communication between ship and shore during
mooring and connecting operations.
The terminal shall install an emergency stand-by oral
communication link. This may be a VHF link.
9.4.2 Data links
For use during LNG transfer, the terminal shall be
equipped with a hard wire data link suitable for
transferring information between ship and shore. A
suitable back up system should be provided for this
data link.
9.5 Firefighting equipment and procedures
9.5.1 Fixed equipment
Both fixed powder and water firefighting equipment
shall be provided.
Fixed fire fighting equipment shall be installed at a
high enough level on the jetty to ensure sufficient
range to reach the highest part of the ship's deck
during the highest tide.
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EN 1532 : 1997
All parts of the Ship/shore Transfer Facility should be
within range of fire fighting equipment. Fire fighting
procedures shall be agreed between the terminal, local
authorities and the ship's crew.
Powder guns may be provided for putting out or
controlling a fire.
The powder supplies are situated at a lower level on
the jetty to protect them from heat radiation during a
fire. A remote control for these guns shall be provided.
(Refer to prEN 1473.)
9.5.2 Portable equipment
Portable fire extinguishers made to the appropriate
standard should be set ready at each berth so that an
outbreak of a small fire can be immediately tackled.
For LNG fires, dry powder extinguishers are suitable
and at least two extinguishers should be available
close to the manifold area during cargo transfer.
Dry powder extinguishers should have a minimum
capacity of 9 kg. They should preferably be
supplemented by larger mobile units (e.g. powder
extinguishers of 50 kg capacity). At other locations on
the terminal where fires could occur (e.g. control
rooms, jetty centres) suitable extinguishers should be
provided.
9.5.3 Water supply
A firefighting water supply is essential for cooling
purposes and can also be used in a fog or spray form
against fires and for screening firefighting personnel. It
can also be used to disperse vapour clouds. The
firemain may be kept dry or charged when no ship is
berthed, but should always be pressurized while LNG
is being transferred. Where necessary, the firemain
should be protected against impact and freezing.
The capacity of the firemain will depend on the flow
rate needed to supply the equipment and to produce
effective jets or sprays of the required reach. Sizing
should be based on the information provided in
prEN 1473.
9.6 Main control room
For the purpose of this standard, the main control
room shall be equipped with:
± the systems for monitoring the cargo transfer
operation;
± the systems for communication with the ship's
cargo control room;
± a visual monitoring system for the transfer
operation;
± a marine VHF station (part of the port network),
the use of which is strictly reserved for sending
safety messages;
± the communications system with the jetty control
centre;
± the arrangements for the ESD;
± the measurement of meteorological data.
9.7 Vapour return system
Volume compensation for the ship's tanks is provided
by vapour return to or from the terminal's storage
tanks. It is transferred through the vapour arm located
in the main manifold area.
Any gas not required onboard ship should be passed to
the vapour recovery systems of the terminal.
Consideration should be given to the following when
designing vapour return systems:
± the maximum gas velocity;
± the pressure;
± the temperature.
9.8 Crew and personnel access (see 7.2.9)
For the purposes of security and safety, terminals
should develop procedures to control visitors and non
company personnel at the jetty and along the approach
roads.
9.9 Motor operated valves (MOV) for ESD
These valves should be as described in 8.3.
9.10 Jetty's electrical safety
All the instrumentation shall be explosion-proof,
intrinsically safe or a certified safe type in accordance
with EN 50014 to EN 50020.
9.11 Ship's storing arrangements
If a crane is provided for the ship's storing, it shall
comply with the appropriate area classification in
which it is operated.
10 LNG transfer procedure
10.1 Necessary provisions prior to ship
acceptance
The ship should hold a valid Certificate of Fitness,
otherwise, it will not be accepted. (In this respect,
reference should be made to the relevant IMO gas
code.)
10.2 Conditions for port entry
The ship is brought up to the jetty, if weather and sea
conditions are considered acceptable by port
authorities, harbour pilot and the ship's master.
Tugs should be available to provide early and effective
assistance. Where necessary, mooring boats and
mooring gangs should be in attendance.
10.3 Conditions to be fulfilled prior to
connecting loading/unloading arms
a) Ship/shore Safety Check List shall be completed
and procedures agreed (see 7.2.4).
b) The LNG cargo quantity on board the ship shall
be calculated.
c) All the necessary documents shall be completed.
d) The ship's manifold should be properly located
within the design operating envelope of the
loading/unloading arms.
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10.4 Conditions to be fulfilled prior to the
transfer of LNG
a) Connection of the loading/unloading arms (the
vapour arm should be connected first).
b) Mutual testing of communication links to ensure
proper operation of the ESD signal and the ERP
operation. All limit switches for ESD functions
should be checked.
c) Connections and safety devices shall be tested.
d) Nitrogen is shown to be flowing through the
swivel joints to prevent them from freezing.
e) Systems, including the loading/unloading arms,
are cooled down, according to a set procedure to
avoid excessive thermal stresses.
10.5 Fulfilment of the safety conditions during
transfer operations
a) Navigation of other ships shall be limited within a
specified zone surrounding the ship and shall be
subject to local rules and regulations.
b) Storing of provisions on the ship is forbidden.
c) Work on the jetty is only carried out under
controlled conditions.
d) The movement of vehicles is controlled within the
jetty area.
The authorization for supplying stores should not be
given during LNG transfer.
Authorization for loading bunkers from the shore may
be given as long as appropriate procedures are
adopted.
10.6 Conditions to be fulfilled following ship's
transfer
On completion of cargo transfer, the disconnection of
loading/unloading arms shall be made only after:
a) all pumps have been stopped;
b) all valves have been closed in accordance with
the agreed procedures;
c) the arms have been cleared of liquid and vapour
and purged with nitrogen;
d) agreement has been reached between ship and
shore staff that the arms can be disconnected.
The liquid arm should be disconnected before the
vapour arm.
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10.7 Shore and ship protection of personnel on
duty
Suitable personal protective equipment should be made
available for those involved in the LNG transfer
operation.
10.8 Responsibilities
10.8.1 Normal procedure
± The ship's mooring operation is controlled by the
ship's master, assisted by the harbour pilot and the
terminal representative positioned on the jetty;
± the connection of the loading/unloading arms is
made by terminal personnel;
± the LNG transfer operation is co-ordinated by both
the ship and the terminal control rooms;
± authorization for the access of visitors on to the
ship is given by the ship's master;
± ship's visitors passing through the terminal need
permission from terminal management.
10.8.2 Emergency procedure
± The ESD can be initiated from either the ship's
cargo control room, the jetty control centre or the
main control room;
± the maintenance of the ERS is the responsibility
of the terminal;
± any quick release of the moorings is only carried
out with the authority of the ship's master when the
ship is ready to leave the jetty.
11 Training of personnel
Training of all staff involved in the monitoring and
handling of LNG shall be provided to enable them to
perform their duties safely and efficiently.
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Annex A (informative)
General safety philosophy
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EN 1532 : 1997
Figure A.1 General safety philosophy for stopping LNG transfer
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EN 1532 : 1997
Annex B (informative)
Bibliography
1.
2.
3.
4.
5.
6.
7.
8.
9.
10.
Safe Transport, Handling and Storage of Dangerous Substances in Port Areas, 1983, IMO.
ISBN 92-801-1160-4.
Mooring Equipment Guidelines, 1992, OCIMF. ISBN 1-85609-088-4.
Guidelines and recommendations for the safe mooring of large Ships at Piers and Sea Islands, 1994,
OCIMF. ISBN 1-85609-054-X.
Recommendations for manifolds for refrigerated Liquefied Natural Gas carriers Ð (LNG) 1994, OCIMF.
ISBN 1-85609-066-3.
Guidelines on the Alleviation of Excessive Surge Pressures on ESD, 1987, SIGTTO. ISBN 0 948691 40 9.
Liquified Gas Handling Principles on Ships and in Terminals, 1995, SIGTTO. ISBN 1-85609-087-6.
International Code for the Construction and Equipment of ships carrying liquified gases in bulk, IMO.
ISBN 92-801-1277-5.
Code for the construction and equipment of ships carrying liquefied gases in bulk, IMO.
ISBN 92-801-1165-5.
ISO 5620-1 Shipbuilding and marine structures Ð Filling connection for drinking water tanks Ð Part 1:
General requirements.
ISO 5620-2 Shipbuilding and marine structures Ð Filling connection for drinking water tanks Ð Part 2:
Components
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BS EN 1532 : 1997
List of references
See national foreword.
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the publications of the international standardization bodies. Except as permitted
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Copyright British Standards Institution
Provided by IHS Markit under license with BSI - Uncontrolled Copy
No reproduction or networking permitted without license from IHS
Licensee=Lloyds Register Group Services/5989898020, User=burgess, floyd
Not for Resale, 06/28/2018 03:25:47 MDT
--`,``,`,,,,,``,,``,``,``,```,`-`-`,,`,,`,`,,`---
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