3.1.1 Care must be exercised when designing piping components for the diving
system to ensure that gas or liquid flow is in the proper direction through the
component. Most components have a designed direction for flow and this should be
observed. Where components permit bi-directional flow, they shall be installed to
take best advantage of the design. For example, valves serving as both inlet and
outlet on high-pressure vessel shall be installed so that when they are closed the
vessel pressure acts from below the seat and not on the valve stem packing.
3.1.2 Piping components shall always be installed in accordance with the
manufacturers' recommendations, unless a deviation is approved by LR.
3.1.3 All manually operated piping system components shall be readily
accessible and easily operable under normal and emergency conditions.
3.1.4 All piping system components shall be selected to permit adequate flow
for the most demanding mission conditions expected for the diving system. These
conditions shall be specified when justifying the selection of a component.
3.1.5 Adequate stop valve and/or check valve protection shall be provided to
prevent loss of control of the system, e.g. isolation valves shall be provided for
all gauges and regulating valves and double valve protection shall be provided on
fill and drain lines for all gas pressure vessel. Double valve protection shall
consist of one isolation valve for each pressure vessel bank and isolation valves
for each pressure vessel in the bank. Pressure vessel drain lines shall be separate
for each individual flask. Flask drain lines shall not be manifolded. Hull and
back-up valves are required on PVHO’s to prevent uncontrolled depressurization or
flooding.
3.1.6 Brazed joints are permitted in copper and copper-alloy piping systems.
Special care must be taken to ensure surface cleanliness and full penetration of the
weld joints in order to prevent entrapment of particulate and eliminate uncleanable
surfaces.
3.1.7 Mechanically attached fittings such as elastic strain preload (ESP),
swaged (Category I UIPI) and shape memory alloy (SMA) types are not permitted in
breathing gas piping systems.
3.1.8 Pipe threads are typically not allowed in life support systems or systems
subjected to external pressure without specific LR approval. Experience has shown
that pipe thread connections are susceptible to corrosion, shock and vibration
damage, and leakage. Consideration must be given to pressure limitations due to a
reduction in wall thickness of the pipe at the tapered threads. Should a component
only be procurable with pipe threaded end fittings, a means must be provided
upstream and downstream of the component to permit its removal without disturbing
the threaded joints. Any compound (e.g. anti-seize thread tape) or lubricant used in
threaded joints shall be suitable for the service conditions.
3.1.9 Flared pipe fittings and their joints shall conform to the range of wall
thickness and method of assembly recommended by the manufacturer. Care should be
taken with cutting and flaring tools so as to not induce work hardening of the tube
end, which can make the material more susceptible to brittle fracture. Flared
fittings are to be of LR type approved.
3.1.10 Flareless, mechanical friction or bite-type connections shall not be used
on piping components where failure could cause uncontrolled depressurization or
flooding of pressure vessels, life support systems, electrical assemblies or other
life-critical components. The use of such fittings in control and monitoring systems
may be permitted only if the component can be quickly isolated from the rest of the
system in case of failure and redundant means of providing the control and
monitoring functions is available; or the fittings are on LR approved equipment.
3.1.11 Fittings where direct impingement of entrained particles may occur, such
as short radius elbows and tees, shall be made from monel. In areas where carbon
steel or stainless steel construction is permitted, fittings with the same
composition may be used if the velocity limit is reduced by half. Piping downstream
of control valves shall be made from monel, for a distance of 10 times the pipe
diameter. For pipe sizes below DN 50, carbon steel shall not be used; stainless
steel shall be used, subject to the velocity limitations given in the Rules and Regulations for the Classification of Ships, July 2022
Pt 5, Ch 12 Piping Design Requirements.
3.1.12 In carbon steel and stainless steel piping systems, branches shall be
made with equal tees, reducing tees or swept outlets. In monel piping systems,
branches should also be made with equal tees, reducing tees or swept outlets, but
branch outlets (weldolets) and branch fittings (nipples) may be used.
3.1.13 Oxygen piping systems shall be kept as simple as possible, with the
smallest possible number of valves, fittings, branches and nozzles. Consideration
should be given to the combination of several instrument connections in one fitting
or nozzle.
3.1.14 Oxygen piping shall be located as far as possible from other piping.
Pipes containing flammable fluid or steam shall not be laid within 1 m distance of
oxygen piping. The free space may be utilised for lines carrying water, nitrogen or
other nonflammable fluids at ambient temperature. At points where the above
requirements cannot be fulfilled, the oxygen system shall be fire protected.
3.1.15 Running of oxygen piping through enclosed spaces should be avoided. If
unavoidable, flanged connections or valves shall not be used and the enclosed space
shall not contain lines carrying flammable fluids. Oxygen piping shall not support
other pipes.
3.1.16 Expansion bellows shall not be used.
3.1.17 In the absence of design justification the following connections shall
not be accepted:
- Slip-on flanges,
- lap flanges,
- socket weld valves and fittings, or
- threaded connections.
3.1.18 Changes in diameter shall be minimised.
3.1.19 Dead ends in piping shall be avoided.
3.1.20 The oxygen flow in piping shall be in one direction only. If flow in two
directions cannot be avoided, arrangements are to be analysed for potential
risks.
3.1.21 To assist removal of the degreasing agent after cleaning, low points in
equipment and piping, shall have drain connections without a valve but closed with a
blind flange or other provisions to remove the cleaning agent, see also
Pt 5, Ch 4, 6 Testing and Cleaning.
3.1.22 Connections for purging and venting shall be situated such that purging
and venting of the system can only be done in the normal direction of the oxygen
flow.
3.1.23 Nitrogen systems used for automatic purging shall be equipped with a
filter and two pressure indicators. They shall be designed to prevent the
possibility of oxygen flowing back into the nitrogen system.