Cargo
Tank Venting and Gas-Freeing Arrangements
8.1 Application
8.1.1 Unless expressly
provided otherwise, this chapter applies to ships constructed on or
after 1 January 1994.
8.1.2 Ships constructed before 1 January 1994 shall comply with the requirements
of chapter 8 of this Code which were in force prior to the
said date.
8.2 Cargo tank venting
8.2.1 All cargo
tanks shall be provided with a venting system appropriate to the cargo
being carried and these systems shall be independent of the air pipes
and venting systems of all other compartments of the ship. Tank venting
systems shall be designed so as to minimize the possibility of cargo
vapour accumulating about the decks, entering accommodation, service
and machinery spaces and control stations and, in the case of flammable
vapours, entering or collecting in spaces or areas containing sources
of ignition. Tank venting systems shall be arranged to prevent entrance
of water into the cargo tanks and, at the same time, vent outlets
shall direct the vapour discharge upwards in the form of unimpeded
jets.
8.2.2 The venting
systems shall be connected to the top of each cargo tank and as far
as practicable the cargo vent lines shall be self-draining back to
the cargo tanks under all normal operational conditions of list and
trim. Where it is necessary to drain venting systems above the level
of any pressure/vacuum valve, capped or plugged drain cocks shall
be provided.
8.2.3 Provision
shall be made to ensure that the liquid head in any tank does not
exceed the design head of the tank. Suitable high-level alarms, overflow
control systems or spill valves, together with gauging and tank filling
procedures, may be accepted for this purpose. Where the means of limiting
cargo tank overpressure includes an automatic closing valve, the valve
shall comply with the appropriate provisions of Ch 1, 15.19 Overflow control.
LR 8.2(a) The system for guarding against
liquid rising to a height which would exceed the design head of the cargo tanks is to be
independent of the gauging devices.
LR 8.2(b) Attention is drawn to the need to
comply with any more onerous filling height restrictions imposed by the carriage of high
relative density cargoes (ie above 1,025).
8.2.4 Tank venting
systems shall be designed and operated so as to ensure that neither
pressure nor vacuum created in the cargo tanks during loading or unloading
exceeds tank design parameters. The main factors to be considered
in the sizing of a tank venting system are as follows:
-
design loading and
unloading rate;
-
gas evolution during
loading: this shall be taken account of by multiplying the maximum
loading rate by a factor of at least 1.25;
-
density of the cargo
vapour mixture;
-
pressure loss in vent
piping and across valves and fittings; and
-
pressure/vacuum settings
of relief devices.
8.2.5 Tank vent
piping connected to cargo tanks of corrosion-resistant material, or
to tanks which are lined or coated to handle special cargoes as required
by the Code, shall be similarly lined or coated or constructed of
corrosion-resistant material.
8.2.6 The master
shall be provided with the maximum permissible loading and unloading
rates for each tank or group of tanks consistent with the design of
the venting systems.
8.3 Types of tank venting systems
8.3.1 An open
tank venting system is a system which offers no restriction except
for friction losses to the free flow of cargo vapours to and from
the cargo tanks during normal operations. An open venting system may
consist of individual vents from each tank, or such individual vents
may be combined into a common header or headers, with due regard to
cargo segregation. In no case shall shutoff valves be fitted either
to the individual vents or to the header.
8.3.2 A controlled
tank venting system is a system in which pressure- and vacuum-relief
valves or pressure/vacuum valves are fitted to each tank to limit
the pressure or vacuum in the tank. A controlled venting system may
consist of individual vents from each tank or such individual vents
on the pressure side only as may be combined into a common header
or headers, with due regard to cargo segregation. In no case shall
shut-off valves be fitted either above or below pressure- or vacuum-relief
valves or pressure/vacuum valves. Provision may be made for bypassing
a pressure- or vacuum-relief valve or pressure/vacuum valve under
certain operating conditions provided that the requirement of Ch 1, 8.3 Types of tank venting systems 8.3.6 is maintained and that there is
suitable indication to show whether or not the valve is bypassed.
8.3.3 Controlled
tank venting systems shall consist of a primary and a secondary means
of allowing full flow relief of vapour to prevent over-pressure or
under-pressure in the event of failure of one means. Alternatively,
the secondary means may consist of pressure sensors fitted in each
tank with a monitoring system in the ship's cargo control room or
position from which cargo operations are normally carried out. Such
monitoring equipment shall also provide an alarm facility which is
activated by detection of over-pressure or under-pressure conditions
within a tank.
8.3.4 The position
of vent outlets of a controlled tank venting system shall be arranged:
-
at a height of not
less than 6 m above the weather deck or above a raised walkway if
fitted within 4 m of the raised walkway; and
-
at a distance of at
least 10 m measured horizontally from the nearest air intake or opening
to accommodation, service and machinery spaces and ignition sources.
8.3.5 The vent
outlet height referred to in Ch 1, 8.3 Types of tank venting systems 8.3.4 may
be reduced to 3 m above the deck or a raised walkway, as applicable,
provided that high-velocity venting valves of an approved type, directing
the vapour/air mixture upwards in an unimpeded jet with an exit velocity
of at least 30 m/s, are fitted.
8.3.6 Controlled
tank venting systems fitted to tanks to be used for cargoes having
a flashpoint not exceeding 60°C (closed-cup test) shall be provided
with devices to prevent the passage of flame into the cargo tanks.
The design, testing and locating of the devices shall comply with
the requirements of the Administration, which shall contain at least
the standards adopted by the Organization.
8.3.7 In designing
venting systems and in the selection of devices to prevent the passage
of flame for incorporation into the tank venting system, due attention
shall be paid to the possibility of the blockage of these systems
and fittings by, for example, the freezing of cargo vapour, polymer
build-up, atmospheric dust or icing up in adverse weather conditions.
In this context it shall be noted that flame arresters and flame screens
are more susceptible to blockage. Provisions shall be made such that
the system and fittings may be inspected, operationally checked, cleaned
or renewed as applicable.
8.4 Venting requirements for individual products
8.4.1 Venting requirements for individual products are shown in column g,
and additional requirements in column o in the table of chapter 17.
8.5 Cargo-tank purging
8.5.1 When the application of inert gas is required by Ch 1, 11.1 Application 11.1.1, before gas-freeing, the cargo
tanks shall be purged with inert gas through outlet pipes with cross-sectional area
such that an exit velocity of at least 20 m/s can be maintained when any three tanks
are being simultaneously supplied with inert gas. The outlets shall extend not less
than 2 m above the deck level. Purging shall continue until the concentration of
hydrocarbon or other flammable vapours in the cargo tanks has been reduced to less
than 2 per cent by volume.
8.6 Cargo-tank gas-freeing
8.6.1 The arrangements
for gas-freeing cargo tanks used for cargoes other than those for
which open venting is permitted shall be such as to minimize the hazards
due to the dispersal of flammable or toxic vapours in the atmosphere
and to flammable or toxic vapour mixtures in a cargo tank. Accordingly,
gas-freeing operations shall be carried out such that vapour is initially
discharged:
-
through the vent outlets
specified in Ch 1, 8.3 Types of tank venting systems 8.3.4 and Ch 1, 8.3 Types of tank venting systems 8.3.5; or
-
through outlets at
least 2 m above the cargo tank deck level with a vertical exit velocity
of at least 30 m/s maintained during the gas-freeing operation; or
-
through outlets at
least 2 m above the cargo tank deck level with a vertical exit velocity
of at least 20 m/s which are protected by suitable devices to prevent
the passage of flame.
When the flammable vapour concentration at the outlets has been
reduced to 30% of the lower flammable limit and, in the case of a
toxic product, the vapour concentration does not present a significant
health hazard, gas-freeing may thereafter be continued at cargo tank
deck level.
8.6.3 In designing
a gas-freeing system in conformity with Ch 1, 8.6 Cargo-tank gas-freeing 8.6.1, particularly in order to achieve the required exit velocities
of Ch 1, 8.6 Cargo-tank gas-freeing 8.6.1.(b) and Ch 1, 8.6 Cargo-tank gas-freeing 8.6.1.(c), due consideration shall be
given to the following:
-
materials of construction
of system;
-
time to gas-free;
-
flow characteristics
of fans to be used;
-
the pressure losses
created by ducting, piping, cargo tank inlets and outlets;
-
the pressure achievable
in the fan driving medium (e.g. water or compressed air); and
-
the densities of the
cargo vapour/air mixtures for the range of cargoes to be carried.
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