9.1 Goal
The goal of this chapter is to ensure safe and reliable distribution of fuel to the
consumers.
9.2 Functional requirements
This chapter is related to functional requirements in 3.2.1 to 3.2.6, 3.2.8 to 3.2.11
and 3.2.13 to 3.2.17. In particular the following apply:
- .1 the fuel supply system shall be so arranged that the consequences of any
release of fuel will be minimized, while providing safe access for operation and
inspection;
- .2 the piping system for fuel transfer to the consumers shall be designed in a
way that a failure of one barrier cannot lead to a leak from the piping system
into the surrounding area causing danger to the persons on board, the
environment or the ship; and
- .3 fuel lines outside the machinery spaces shall be installed and protected so
as to minimize the risk of injury to personnel and damage to the ship in case of
leakage.
9.3 Regulations on redundancy of
fuel supply
9.3.1 For single fuel installations the fuel supply system shall be
arranged with full redundancy and segregation all the way from the fuel tanks to the
consumer, so that a leakage in one system does not lead to an unacceptable loss of
power.
LR 9.3-01 For single fuel installations, a system dependability
assessment is to be undertaken. The objectives of the assessment are to:
(a) demonstrate the dependability of the system during all normal and
reasonably foreseeable abnormal conditions where essential services are reliant upon
the system for their intended operation; and,
(b) demonstrate that an appropriate level of dependability is achieved
that is commensurate with conventional oil fuelled machinery.
The scope of the assessment is to consider:
(a) the redundancy of fuel storage and supply; and,
(b) the reliability and availability of machinery, equipment and
components to maintain essential services.
The assessment is to be undertaken to a recognised Standard acceptable
to LR, such as IEC 60300-3-1, Dependability management Part 3-1: Application guide –
Analysis techniques for dependability – Guide on methodology.
9.3.2 For single fuel installations, the fuel storage shall be divided between two or
more tanks. The tanks shall be located in separate compartments.
9.3.3 For type C tank only, one tank may be accepted if two completely separate tank
connection spaces are installed for the one tank.
9.4 Regulations on safety
functions of gas supply system
9.4.1 Fuel storage tank inlets and outlets shall be provided with valves
located as close to the tank as possible. Valves required to be operated during
normal operationfootnote which are not accessible shall be
remotely operated. Tank valves whether accessible or not shall be automatically
operated when the safety system required in 15.2.2 is activated.
9.4.2 The main gas supply line to each gas consumer or set of consumers
shall be equipped with a manually operated stop valve and an automatically operated
"master gas fuel valve" coupled in series or a combined manually and automatically
operated valve. The valves shall be situated in the part of the piping that is
outside the machinery space containing gas consumers, and placed as near as possible
to the installation for heating the gas, if fitted. The master gas fuel valve shall
automatically cut off the gas supply when activated by the safety system required in
15.2.2.
9.4.3 The automatic master gas fuel valve shall be operable from safe
locations on escape routes inside a machinery space containing a gas consumer, the
engine control room, if applicable; outside the machinery space, and from the
navigation bridge.
9.4.4 Each gas consumer shall be provided with "double block and bleed"
valves arrangement. These valves shall be arranged as outlined in .1 or .2 so that
when the safety system required in 15.2.2 is activated this will cause the shutoff
valves that are in series to close automatically and the bleed valve to open
automatically and:
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.1 the two shutoff valves shall be in series in the gas fuel pipe
to the gas consuming equipment. The bleed valve shall be in a pipe that
vents to a safe location in the open air that portion of the gas fuel piping
that is between the two valves in series; or
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.2 the function of one of the shutoff valves in series and the
bleed valve can be incorporated into one valve body, so arranged that the
flow to the gas utilization unit will be blocked and the ventilation opened.
9.4.5 The two valves shall be of the fail-to-close type, while the
ventilation valve shall be fail-to-open.
9.4.6 The double block and bleed valves shall also be used for normal
stop of the engine.
9.4.7 In cases where the master gas fuel valve is automatically shutdown,
the complete gas supply branch downstream of the double block and bleed valve shall
be automatically ventilated assuming reverse flow from the engine to the pipe.
LR 9.4-01 There shall be separate vent lines from areas such as
gas fuel tanks and gas consumers (engines etc.) that are independent of each other.
Bleed lines shall also be independent of the vent lines. Such vent and bleed lines
shall not be connected to a common header unless they are from a same area.
9.4.8 There shall be one manually operated shutdown valve in the gas
supply line to each engine upstream of the double block and bleed valves to assure
safe isolation during maintenance on the engine.
9.4.9 For single-engine installations and multi-engine installations,
where a separate master valve is provided for each engine, the master gas fuel valve
and the double block and bleed valve functions can be combined.
9.4.10 For each main gas supply line entering an ESD protected machinery
space, and each gas supply line to high pressure installations means shall be
provided for rapid detection of a rupture in the gas line in the engine-room. When
rupture is detected a valve shall be automatically shut off.footnote This valve shall be located in the gas
supply line before it enters the engine-room or as close as possible to the point of
entry inside the engine-room. It can be a separate valve or combined with other
functions, e.g. the master valve.
9.5 Regulations for fuel distribution outside of machinery space
9.5.1 Where fuel pipes pass through enclosed spaces in the ship, they shall be
protected by a secondary enclosure. This enclosure can be a ventilated duct or a
double wall piping system. The duct or double wall piping system shall be
mechanically underpressure ventilated with 30 air changes per hour, and gas
detection as required in 15.8 shall be provided. Other solutions providing an
equivalent safety level may also be accepted by the Administration.
9.5.2 The requirement in 9.5.1 need not be applied for fully welded fuel gas vent
pipes led through mechanically ventilated spaces.
9.6 Regulations for fuel supply to consumers in gas-safe machinery spaces
9.6.1 Fuel piping in gas-safe machinery spaces shall be completely enclosed by a
double pipe or duct fulfilling one of the following conditions:
- .1 the gas piping shall be a double wall piping system with the gas fuel
contained in the inner pipe. The space between the concentric pipes shall be
pressurized with inert gas at a pressure greater than the gas fuel pressure.
Suitable alarms shall be provided to indicate a loss of inert gas pressure
between the pipes. When the inner pipe contains high pressure gas, the system
shall be so arranged that the pipe between the master gas valve and the engine
is automatically purged with inert gas when the master gas valve is closed;
or
- .2 the gas fuel piping shall be installed within a ventilated pipe or duct. The
air space between the gas fuel piping and the wall of the outer pipe or duct
shall be equipped with mechanical underpressure ventilation having a capacity of
at least 30 air changes per hour. This ventilation capacity may be reduced to 10
air changes per hour provided automatic filling of the duct with nitrogen upon
detection of gas is arranged for. The fan motors shall comply with the required
explosion protection in the installation area. The ventilation outlet shall be
covered by a protection screen and placed in a position where no flammable
gas-air mixture may be ignited; or
- .3 other solutions providing an equivalent safety level may also be accepted by
the Administration.
9.6.2 The connecting of gas piping and ducting to the gas injection
valves shall be completely covered by the ducting. The arrangement shall facilitate
replacement and/or overhaul of injection valves and cylinder covers. The double
ducting is also required for all gas pipes on the engine itself, until gas is
injected into the chamber.footnote
9.7 Regulations for gas fuel supply to consumers in ESD-protected machinery
spaces
9.7.1 The pressure in the gas fuel supply system shall not exceed 1.0 MPa.
9.7.2 The gas fuel supply lines shall have a design pressure not less than 1.0
MPa.
9.8 Regulations for the design of ventilated duct, outer pipe against inner pipe
gas leakage
9.8.1 The design pressure of the outer pipe or duct of fuel systems shall not be less
than the maximum working pressure of the inner pipe. Alternatively for fuel piping
systems with a working pressure greater than 1.0 MPa, the design pressure of the
outer pipe or duct shall not be less than the maximum built-up pressure arising in
the annular space considering the local instantaneous peak pressure in way of any
rupture and the ventilation arrangements.
9.8.2 For high-pressure fuel piping the design pressure of the ducting shall be taken
as the higher of the following:
-
.1 the maximum built-up pressure: static pressure in way of the rupture
resulting from the gas flowing in the annular space;
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.2 local instantaneous peak pressure in way of the rupture: this pressure
shall be taken as the critical pressure given by the following
expression:
![](svgobject/CDA4-4F2B-A306-C6DBBCBBC1E5.xml_d9778347e256.png)
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where:
The tangential membrane stress of a straight pipe shall not exceed the tensile
strength divided by 1.5 (Rm/1.5) when subjected to the above pressures.
The pressure ratings of all other piping components shall reflect the same level of
strength as straight pipes.
As an alternative to using the peak pressure from the above formula, the peak
pressure found from representative tests can be used. Test reports shall then be
submitted.
9.8.3 Verification of the strength shall be based on calculations demonstrating the
duct or pipe integrity. As an alternative to calculations, the strength can be
verified by representative tests.
9.8.4 For low pressure fuel piping the duct shall be dimensioned for a design
pressure not less than the maximum working pressure of the fuel pipes. The duct
shall be pressure tested to show that it can withstand the expected maximum pressure
at fuel pipe rupture.
9.9 Regulations for compressors and pumps
9.9.1 If compressors or pumps are driven by shafting passing through a bulkhead or
deck, the bulkhead penetration shall be of gastight type.
9.9.2 Compressors and pumps shall be suitable for their intended purpose. All
equipment and machinery shall be such as to be adequately tested to ensure
suitability for use within a marine environment. Such items to be considered would
include, but not be limited to:
- .1 environmental;
- .2 shipboard vibrations and accelerations;
- .3 effects of pitch, heave and roll motions, etc.; and
- .4 gas composition.
9.9.3 Arrangements shall be made to ensure that under no circumstances liquefied gas
can be introduced in the gas control section or gas-fuelled machinery, unless the
machinery is designed to operate with gas in liquid state.
9.9.4 Compressors and pumps shall be fitted with accessories and instrumentation
necessary for efficient and reliable function.
LR 9.9-01 Each size and type of liquefied fuel gas pump is to be
approved through prototype testing and is to include a hydrostatic test of the pump
body equal to 1,5 times the design pressure and a capacity test. For submerged
electric motor driven pumps, the capacity test is to be carried out with the design
medium or with a medium below the minimum working temperature. For shaft driven deep
well pumps, the capacity test may be carried out with water. In addition, for shaft
driven deep well pumps, a spin test to demonstrate satisfactory operation of bearing
clearances, wear rings and sealing arrangements is to be carried out at the minimum
design temperature. The full length of shafting is not required for the spin test,
but must be of sufficient length to include at least one bearing and sealing
arrangement. On completion of testing, the pump is to be opened out for examination.
Prototype testing is to be completed to the satisfaction of the LR Surveyor. In lieu
of prototype testing, satisfactory in-service experience of an existing pump design
approved by a Classification Society submitted by the manufacturer may be
considered.
LR 9.9-02 All liquefied fuel gas pumps are to be tested at the
manufacturer’s works to the satisfaction of the LR Surveyor. Testing is to include a
hydrostatic test of the pump body equal to 1,5 times the design pressure and a
capacity test. For submerged electric motor driven pumps, the capacity test is to be
carried out with the design medium or with a medium below the minimum working
temperature. For shaft driven deep well pumps, the capacity test may be carried out
with water. Alternatively, if so requested by the relevant manufacturer, the
certification of a pump may be issued subject to the following:
(a) the pump has been approved in accordance with the requirements in LR
9.9-01;
(b) the manufacturer has a recognised quality system that has been
assessed and certified by LR in accordance with the requirements of Pt 5, Ch 1,6 of
the Rules for Ships; and,
(c) a quality control plan is submitted which contains a provision to
subject each pump to a hydrostatic test of the pump body equal to 1,5 times the
design pressure and a capacity test. The manufacturer is to maintain records of such
tests.