2.5.1 The requirements of this section apply to
gas piping. The Administration may accept relaxation from these requirements
for gas piping inside gas tanks and open-ended piping after special
consideration, such as risk assessment.
2.5.2 Gas piping should be protected against mechanical
damage and the piping should be capable of assimilating thermal expansion
without developing substantial tension.
2.5.3 The piping system should be joined by welding
with a minimum of flange connections. Gaskets should be protected
against blow-out.
2.5.4 The wall thickness of pipes should not be
less than:
where:
t
0
|
= |
theoretical thickness |
t
0
|
= |
pD/(20Ke + p)
|
where:
p |
= |
design pressure
(bar), refer to 2.5.5. |
D
|
= |
outside
diameter (mm). |
K
|
= |
allowable
stress (N/mm2), refer to 2.5.6.
|
e
|
= |
efficiency
factor equal to 1 for seamless pipes and for longitudinally or spirally
welded pipes, delivered by approved manufacturers of welded pipes,
which are considered equivalent to seamless pipes when non-destructive
testing on welds is carried out in accordance with recognized standards.
In other cases an efficiency factor value depending on the manufacturing
process may be determined by the Administration. |
b
|
= |
allowance
for bending (mm). The value of b should be chosen so that the calculated
stress in the bend, due to internal pressure only, does not exceed
the allowable stress. Where such justification is not give, b should
be:
|

with:
r
|
= |
mean
radius of the bend (mm). |
c
|
= |
corrosion
allowance (mm). If corrosion allowance or erosion is expected, the
wall thickness of the piping should be increased over that required
by other design requirements. This allowance should be consistent
with the expected life of the piping. |
a
|
= |
negative
manufacturing tolerance for thickness (%). |
The minimum wall thickness should be in accordance with recognized
standards.
2.5.5 The greater of the following design conditions
should be used for piping, piping system and components as appropriate:
-
.1 for systems or components which may be separated
from their relief valves and which contain only vapour at all times,
the superheated vapour pressure at 45°C or higher or lower if
agreed upon by the Administration (refer to IGC Code, paragraph 4.2.6.2), assuming an initial
condition of saturated vapour in the system at the system operating
pressure and temperature; or
-
.2 the MARVS of the gas tanks and gas processing
systems; or
-
.3 the pressure setting of the associated pump
or compressor discharge relief valve if of sufficient capacity; or
-
.4 the maximum total discharge or loading head
of the gas piping system; or
-
.5 the relief valve setting on a pipeline system
if of sufficient capacity; or
-
.6 a pressure of 10 bar except for open-ended
lines where it is not to be less than 5 bar.
2.5.6 For pipes made of steel including stainless
steel, the allowable stress to be considered in the formula of the
strength thickness in 2.5.4 should be the lower of the following values:
where:
R
m
|
= |
specified minimum tensile strength at room temperature (N/mm2).
|
R
e
|
= |
specified lower minimum yield stress or 0.2% proof stress at
room temperature (N/mm2).
|
A
|
= |
2.7. |
B
|
= |
1.8. |
For pipes made of materials other than steel, the allowable
stress should be considered by the Administration.
2.5.7 Where necessary for mechanical strength
to prevent damage, collapse, excessive sag or buckling of pipe due
to superimposed loads from supports, ship deflection or other causes,
the wall thickness should be increased over that required by 2.5.4
or, if this is impractical or would cause excessive local stresses,
these loads should be reduced, protected against or eliminated by
other design methods.
2.5.8 Gas piping systems should have sufficient
constructive strength. For high pressure gas piping systems this should
be confirmed by carrying out stress analysis and taking into account:
-
.1 stresses due to the weight of the piping system;
-
.2 acceleration loads when significant; and
-
.3 internal pressure and loads induced by hog
and sag of the ship.
2.5.9 Flanges, valves, fittings, etc., should
be in accordance with recognized standards taking into account the
design pressure defined in 2.5.5. For bellows and expansion joints
used in vapour service, a lower minimum design pressure than defined
in 2.5.5 may be accepted.
2.5.10 All valves and expansion joints used in
high pressure gas systems should be of an approved type.
2.5.11 The following types of connections may
be considered for direct connection of pipe lengths (without flanges):
-
.1 Butt welded joints with complete penetration
at the root may be used in all applications. For design temperature
below -10°C, butt welds should be either double welded or equivalent
to a double welded butt joint. This may be accomplished by use of
a backing ring, consumable insert or inert gas back-up on the first
pass. For design pressures in excess of 10 bar and design temperatures
-10°C or lower, backing rings should be removed.
-
.2 Slip-on welded joints with sleeves and related
welding, having dimensions satisfactory to the Administration, should
only be used for open-ended lines with external diameter of 50 mm
or less and design temperatures not lower than -55°C.
-
.3 Screwed couplings should only be used for accessory
lines and instrumentation lines with external diameters of 25 mm or
less.
2.5.12 Flanges should be of the welding neck,
slip-on or socket welding type. For all piping (except open-ended
lines), the following apply:
-
.1 For design temperatures < -55°C only
welding neck flanges should be used.
-
.2 For design temperatures < -10°C slip-on
flanges should not be used in nominal sizes above 100 mm and socket
welding flanges should not be used in nominal sizes above 50 mm.
2.5.13 Piping connections other than those mentioned
above may be accepted upon consideration in each case.
2.5.14 Postweld heat treatment should be required
for all butt welds of pipes made with carbon, carbon-manganese and
low-alloy steels. The Administration may waive the requirement for
thermal stress relieving of pipes having wall thickness less than
10 mm in relation to the design temperature and pressure of the piping
system concerned.
2.5.15 When the design temperature is -110°C
or lower, a complete stress analysis for each branch of the piping
system should be submitted. This analysis should take into account
all stresses due to weight of pipes with cargo (including acceleration
if significant), internal pressure, thermal contraction and loads
induced by movements of the ship. For temperatures above -110°C,
a stress analysis may be required by the Administration. In any case,
consideration should be given to thermal stresses, even if calculations
need not be submitted. The analysis should be carried out according
to a recognized code of practice.
2.5.16 Gas pipes should not be located less than
760 mm from the ships side.
2.5.17 Gas piping should not be led through other
machinery spaces. Alternatively, double gas piping may be approved,
provided the danger of mechanical damage is negligible, the gas piping
has no discharge sources and the room is equipped with a gas alarm.
2.5.18 An arrangement for purging gas bunkering
lines and supply lines (only up to the double block and bleed valves
if these are located close to the engine) with nitrogen should be
provided.
2.5.19 The gas piping system should be installed
with sufficient flexibility. Arrangement for provision of the necessary
flexibility should be demonstrated to maintain the integrity of the
piping system in all foreseen service situations.
2.5.20 Gas pipes should be colour marked based
on a recognized standardfootnote.
2.5.21 If the fuel gas contains heavier components
that may condense in the system, knock out drums or equivalent means
for safely removing the liquid should be fitted.
2.5.22 All pipelines and components which may
be isolated containing liquid gas should be provided with relief valves.
2.5.23 Where tanks or piping are separated from
the ship's structure by thermal isolation, provision should be made
for electrically bonding to the ship's structure both the piping and
the tanks. All gasketed pipe joints and hose connections should be
electrically bonded.