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LNG Carriers - Membrane Construction
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LNG Carriers Advantages of Membrane Technology
1
Pressure Vessel Engineering
LNG vessel construction –
Advantages of membrane technology
The arrangement for containment of
cargo including, where fitted, a primary and
secondary barrier, associated insulation and
any intervening spaces, and adjacent
structure, if necessary for the support of
these elements. If the secondary barrier is
part of the hull structure it may be a
boundary of the hold space.
To contain LNG cargo at cryogenic
temperatures (-160 0C).
To insulate the cargo from the hull
structure.
The materials used for the hull structure
are designed to withstand varying degrees
of temperature. At temperatures below their
specified limits, these steels will crystallise
and become brittle. The materials used for
the containment system are required to
reduce the heat transfer from the hull
structure to minimise boil-off gas from the
cargo, as well as to protect the hull structure
from the effects of cryogenic temperatures.
MEMBRANE CARGO CONTAINMENT
The cargo containment system consists
of insulated cargo tanks encased within the
inner hull and situated in-line from forward
to aft. The spaces between the inner hull
and outer hull are used for ballast and will
LNG Carriers Advantages of Membrane Technology
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Pressure Vessel Engineering
also protect the cargo tanks in the event of
an emergency situation, such as collision or
grounding.
The cargo tanks are separated from
other compartments, and from each other,
by transverse cofferdams which are dry
compartments.
The following description is of a Gaz
Transport GT96 double membrane system
design. Although the principal design
features will be similar in other systems, e.g.
Technigaz, there will be differences in
membrane construction and insulation
structure.
In the Gaz Transport GT96 design, the
inner hull, that is, the outer shell of each of
the cargo tanks, is lined internally with the
patent tank containment and insulation
system. This consists of the following:
1. A thin flexible membrane, called the
primary membrane, which is in contact
with the cargo. This is fabricated from
Invar and has a typical thickness of
0.7mm.
2. A layer of plywood boxes filled with
Perlite, called the primary insulation,
typically of approximately 230 mm
thickness.
3. A second flexible membrane similar to
the first one, called the secondary
membrane. Also of Invar and having a
typical thickness of 0.7mm.
4. A second layer of boxes, also filled with
Perlite, and in contact with the inner
hull, called the secondary insulation.
This layer is typically of approximately
300 mm thickness.
The tank lining thus consists of two
identical layers of membrane and insulation,
so that in the event of a leak in the primary
barrier, the cargo will be contained by the
secondary barrier. The secondary barrier is
only designed to contain any envisaged
leakage of cargo for a period of 15 days.
(IGC Chapter 1V 4.7.4). This system
ensures that all the hydrostatic loads of the
cargo are transmitted through the
membranes and insulation to the inner hull
plating of the ship.
Fig: Membrane design
LNG Carriers Advantages of Membrane Technology
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Pressure Vessel Engineering
The function of the membranes is to
prevent leakage, while the insulation
supports and transmits the loads and, in
addition, minimises heat exchange between
the cargo and the inner hull. The secondary
membrane, sandwiched between the two
layers of insulation, not only provides a
safety barrier between the two layers of
insulation, but also reduces convection
currents within the insulation.
The primary and secondary insulation
spaces are maintained under a pressure-
controlled nitrogen atmosphere. The
pressure of nitrogen within the primary
space must never exceed the cargo tank
pressure, in order to prevent the membrane
from collapsing inwards. The insulation
design should ensure that:
1. The heat flow into the tank is limited to
such an extent that the evaporation, or
boil-off rate, is about 0.15% per day
based on sea surface temperature of
32 degrees and air temperature 45
degrees Celsius.
2. The inner hull steel does not attain a
temperature below its minimum design
value, even in the case of failure of the
primary barrier.
3. Any deflections resulting from applied
strains and stresses are acceptable by
the primary barrier.
In addition to the above, the insulation
acts as a barrier to prevent any contact
between ballast water and the primary
barrier, in the event of leakage through the
inner hull.
DETERIORATION OR FAILURE OF
INSULATION SYSTEM
The insulation system is designed to
maintain the boil-off losses from the cargo
at an acceptable level, and to protect the
inner hull steel from the effect of excessively
low temperature. If the insulation efficiency
should deteriorate for any reason, the effect
may be a lowering of the inner hull steel
temperature, i.e. a cold spot and an
increase in boil-off from the affected tank. If
necessary, increased boil-off gas may be
vented to the atmosphere via the vent riser
and gas heater. The inner hull steel
temperature must, however, be maintained
within acceptable limits to prevent possible
brittle fracture.
Thermocouples are normally distributed
over the surface of the inner hull, but unless
a cold spot occurs immediately adjacent to
a sensor, these can only serve as a general
indication of steel temperature. To date, the
only reliable way of detecting cold spots is
by frequent visual inspections of the ballast
spaces on the loaded voyage.
LNG Carriers Advantages of Membrane Technology
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Pressure Vessel Engineering
In addition to failure of the membrane,
local cold spots can occur due to failure of
the insulation. While the inner hull steel
quality has been chosen to withstand the
minimum temperature likely to occur in
service, prolonged operation at steel
temperatures below 0°C will cause ice build-
up on the plating, which in turn will cause a
further lowering of steel temperature due to
the insulating effect of the ice. To avoid this,
heating coils may be fitted in the cofferdam
spaces, of sufficient capacity to maintain the
inner hull steel temperature at 0°C under
the worst conditions.
If a cold spot is detected, either by the
inner hull temperature measurement
system, or by visual inspection, the extent
and location of the ice formation should be
recorded. Small local cold spots are not
critical and, provided a close watch and
record are kept as a check against further
deterioration and spreading of the ice
formation, no further action is required. If
the cold spot is extensive, or tending to
spread rapidly, salt water spraying should
be carried out.
In the unlikely event that this remedy is
insufficient and it is considered unsafe to
delay discharge of cargo until arrival at the
discharge port, the final recourse will be to
jettison the cargo via a spool piece fitted at
the cargo liquid manifold, using a single
main cargo pump. This action should only
be taken after full consultation with the
Managing Office and relevant authorities.
INNER HULL INSPECTIONS (MEMBRANE
HULL CONTAINMENT)
It is a requirement that all spaces
around the cargo tanks are inspected at
least once in every six month period. To
meet this requirement the inner hull around
a nominated cargo tank is inspected from
the ballast tank, cofferdam, and whaleback
areas (including the whaleback areas
external to the ballast tank), each alternate
passage. This frequency ensures every
space is inspected within the required
period.
These inspections should commence
approximately 48 hours after a cargo is
loaded. The following points are to be
covered and recorded.
1. The position and temperature of cold
spots or absence of cold spots.
2. Condition of anodes.
3. Condition of paintwork - a reference
sheet is provided for this.
4. Extent of corrosion on both the inner
and outer hulls, particularly under the
suction strums, in the way of striking
LNG Carriers Advantages of Membrane Technology
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Pressure Vessel Engineering
plates and behind heating coils in the
ballast and cofferdams.
5. Position and amount of sediment.
6. Any damage, fractures etc. Particular
attention to be paid to the external
portion of the inner hull for evidence of
fractures, and to the turn of the bilge
areas of the inner hull within the
midships section of the vessel.
7. Hydraulic or heating coil leaks and the
condition of scupper pipes. The duct
keel is to be inspected every six months
and must be well ventilated by fan
before entry. All spaces should be
inspected on the first cargo after a dry-
dock period. The void space around
each of the liquid domes should be
included in the inspection of the spaces
around the nominated cargo tank.
NOTE: It is a Classification requirement for
the granting of a valid Certificate of Fitness
for ships carrying liquefied gases in bulk
that routine cold spot inspections are carried
and recorded.
Fig: MEMBRANE DESIGN – GAS TRANSPORT TECHNIGAZ (GTT) –GT96
*********
Source : Scrapped from liquefiedgascarriers.com