Section
9 Piping for LPG/LNG carriers, gas fuelled ships and classed refrigeration
systems
9.1 Scope
9.1.1 This
Section is applicable to piping systems installed in LPG/LNG carriers,
gas fuelled ships and classed refrigeration systems for the following
pipes and piping system components:
-
Pipework –
stainless steel, carbon steel and copper.
-
Valves –
normal and cryogenic service (below minus 55°C).
-
Bellows –
normal and cryogenic service (below minus 55°C).
-
Pipe fittings
– elbows, reducers, tee connections, etc.
-
Ancillary fittings
– weldolets, threadolets, thermopockets.
9.1.2 The
following piping systems are covered by this Section:
-
LPG/LNG cargo
systems – normal cargo operations.
-
LPG/LNG cargo
systems – cargo gas to reliquefaction system.
-
LNG cargo systems
– gas burning and use of cargo as fuel.
-
LNG Regasification
system – high and low pressure.
-
Cargo Reliquefaction
system – nitrogen or mixed refrigerant.
-
Refrigeration
– independent plant used in cascade systems.
-
Gas storage and
supply systems for gas fuelled ships.
9.2 Application
9.2.1 The
requirements of this Section apply to pipes and piping system components,
such as valves, elbows and bellows, which are to be used on gas carriers,
gas fuelled ships or classed refrigeration/reliquefaction systems.
The requirements are also applicable to other gas cargo services such
as regasification systems and gas combustion units, and are in addition
to those contained in both the Rules for Ships for Liquefied Gases
and relevant Sections of this Chapter where appropriate.
9.3 Classes of piping system and components
9.3.1 The material requirements for piping systems vary depending on the Class of
the piping system. The Class of the piping system is dependent on the design pressure or
temperature of the system and the pipe material used, see
Pt 5, Ch 12, 1.6 Classes of piping systems and components.
9.3.2
Table 12.1.1 Maximum pressure and temperature
conditions for Class II and III piping systems shows piping systems containing LPG/LNG,
cargo or fuel gas as the conveyed medium are to be treated as 'Flammable liquids'. These
piping systems are to be categorised as Class II. Vapour lines are also to be
categorised as Class II systems but the upper limit on pressure may be increased to 4
MPa gauge in accordance with the ‘Other media’. Where higher design pressures are
applied, such as in a regasification system, liquid lines above 1,6 MPa gauge and vapour
lines above 4 MPa gauge are to be categorised as Class I. All open ended pipes, such as
vent lines and pipes inside the cargo tanks may be categorised as Class III, provided
that the temperature of the cargo at the pressure relief valve setting is not colder
than minus 55°C.
9.3.3 For reliquefaction and refrigeration systems the requirements of Pt 5, Ch 12, 1.6 Classes of piping systems and components are to be applied.
Nitrogen and non-toxic or nonflammable refrigerants are to be considered under the
‘Other media’ heading. Refrigeration systems containing ammonia are to be considered as
Class I systems irrespective of the operational pressure.
9.4 Materials
9.4.3 For stainless steel pipes, valve castings and forgings, a manufacturer’s
certificate is acceptable where the intended service temperature is not colder than
minus 55°C and:
-
DN <50 or
-
DN ≤150 and DN x P <250
Where:
DN = nominal diameter, mm
P = design
pressure, in MPa gauge
In all other cases, an LR materials certificate is required.
9.5 Valves and piping components independent of temperature
9.5.1 For
valves and piping components fitted in the cargo piping system of
LPG/LNG gas carriers, each type of valve and piping component is to
have evidence of satisfactory type testing.
9.6 Valves for cryogenic temperature service
9.6.1 Each
size and type of valve intended to be used at a working temperature
below –55°C shall be approved. Approval is based upon prototype
testing and assessment of the design for compliance with a recognised
national or international standard acceptable to LR.
9.7 Valves for refrigeration service
9.7.1 For
valves intended for installation in a refrigeration system with a
nominal diameter equal to or less than 150 mm, a manufacturer’s
certificate is acceptable. The certificate is to include details of
the maximum working pressure and test pressure, and sufficient information
for the LR Surveyor to assess the suitability of the equipment for
the intended use. Each size and type of valve is to be supplied with
its own certificate and is to be signed by a responsible person in
the manufacturer’s quality control department.
9.7.2 Valves
with nominal diameters above 150 mm are to be supplied with a LR materials
certificate in accordance with the Rules for Materials.
9.7.4 Any
valve fitted directly onto a pressure vessel is to be considered a
mounting and is required to be hydraulically pressure tested to twice
the approved design pressure. See
Pt 5, Ch 11, 10.2 Mountings 10.2.1.
9.8 Expansion bellows
9.8.3 For each type of expansion bellows, an element of the bellows, not
pre-compressed, is to be pressure tested at not less than five times the design pressure
without bursting. This test is to be conducted at room temperature on each ‘type’ of
element and need not be the complete bellows unit. A test on one element can cover other
sized bellows with the same cross-sectional bellows form. The design pressure is to be
at least 1 MPa gauge; bellows fitted to safety valves and vent lines may have a minimum
design pressure of not less than the lower of 0,5 MPa gauge or 10 times the relief valve
set pressure in accordance with Process Pressure Vessels and Liquid, Vapour and Pressure Piping Systems of the Rules for Ships for Liquefied Gases. The required test
duration is not to be less than 5 minutes.
9.8.4 A pressure
test is to be performed on each type of expansion joint complete with
all the accessories such as flanges, stays and articulations, at twice
the design pressure at the extreme displacement conditions recommended
by the manufacturer without permanent deformation. The test is to
be undertaken at the minimum design temperature, unless the bellows
material is stainless steel for which this test may be carried out
at ambient temperature. The test duration is to be 30 minutes unless
otherwise agreed with LR.
9.8.5 A cyclic
thermal movement test, replicating the cooling down and warming up
cycle which occurs during cargo loading and discharge, is to be performed
on a complete expansion joint, by the application of representative
external deflection resulting in bellow movement. This is to successfully
withstand at least as many cycles, under the conditions of pressure,
temperature, axial movement, rotational movement and transverse movement,
as it will encounter in actual service. The number of cycles is to
be estimated by the builder and depends on the ship’s intended
trading pattern and life expectancy. As a minimum, testing to 7000
cycles is to be carried out. The test is to be carried out at between
2-5 cycles per second. Testing at ambient temperature is permitted
when this testing is at least as severe as testing at the service
temperature. The maximum movements on the horizontal and vertical
axis are to be provided by the builders and obtained from their stress
analysis; however, the test can be extended to any value which is
greater than that expected, or to the maximum deflection for which
the bellows unit is suitable. Movements in the test need not be in
both horizontal and vertical directions; but the horizontal-vertical
box diagonal distance may be used. NDE testing is required after cyclic
testing.
9.8.6 A cyclic fatigue test, representing ship deformation, is to be performed on
a complete expansion joint (inclusive of its thermal insulation when fitted, where the
thermal insulation is an integral part of the joint; however, this test could be
performed without insulation where the thermal insulation is completely independent of
the bellows movement), without internal pressure, by simulating the bellows movement
corresponding to a compensated pipe length, for at least 2,000,000 cycles at a frequency
not higher than 5 Hz. NDE is required after cyclic testing. This test is only required
when, due to the piping arrangement, ship deformation loads are actually experienced.
9.9 Pressure testing of piping and other piping components
9.9.1 Pressure
testing is to be undertaken in accordance with specific Rule requirements
relating to the system in which the component is to be located.
9.9.2 The
duration for which pressure tests are to be held is to be in conjunction
with an applicable and recognised code or standard acceptable to LR.
9.10 Equipment documentation
9.10.1 A
certificate is required for each piping component supplied to be fitted
in a Class I or Class II system. This certification is required for
each size and type of equipment delivered. A single certificate may
cover a number of valves, provided that they are of the same type
and size, and serial numbers have been included on the certificate.
If the piping components are part of a system fitted to a skid or
packaged unit, then the complete skid may be supplied with a single
certificate stating that the package has been constructed using approved
materials, approved and tested in accordance with LR Rule requirements.
9.11 Relief valves for LPG/LNG cargo and deck tanks
9.11.1 Relief
valves fitted to cargo tanks and deck tanks are to be of a type tested
design. Type testing is to include:
- flow or capacity verification to a recognised Standard acceptable
to the Administration;
- cryogenic testing when operating at design temperatures colder
than minus 55°C;
- seat tightness testing to a recognised Standard or manufacturers’
procedure acceptable to the Administration; and
- pressure testing of pressure-containing parts to at least 1,5
times the design pressure.
9.11.2 The
materials used for construction of relief valves fitted to cargo tanks
and deck tanks are to be produced in a works approved by LR and be
provided with a Clasifications Register Material Certificate.
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