Section
2 Minimum requirements
2.1 General
2.1.3 Where a ship, by virtue of its gross tonnage, is not required by the
Antifouling Convention to have certification, an antifouling system (AFS) declaration in
the format shown in Appendix 2 of Annex 4 to the Convention is to be maintained on
board. The application of antifouling systems containing TBT above the level specified
in the Antifouling Convention is prohibited.
2.1.6 Offshore supply vessels that are less than 100 m in length, as per MSC
235(82), are exempt from the requirement to be enrolled in LR’s Ship Emergency Response
Service (SERS) or the equivalent scheme of another IACS member. Exempting the
requirement for enrolment in SERS, or the equivalent scheme of another IACS member for
other vessel types, will be specially considered depending on the vessel’s size and
operational profile.
2.2 Nitrogen oxides (NOx)
2.2.1 These
requirements apply to all installed diesel engines with an individual
output power greater than 130 kW, other than those used solely for
emergency purposes on the ship on which the engine is installed. There
are no specific requirements relating to NOx emissions
from boilers, incinerators or gas turbine installations.
2.2.2 All
engines falling within the scope of MARPOL Annex VI, Regulation 13 – Nitrogen Oxides (NOx) are to comply with its
provisions and meet the NOx emission limits applicable
to the date of construction of the ship or, where relevant, the engine
installation date.
2.2.3
EIAPP certification or Statement of Compliance is to be issued by,
or on behalf of, the Flag State.
2.2.4 Alternative
arrangements providing an equivalent level of environmental protection
will be considered.
2.3 Sulphur oxides (SOx)
2.3.1 Emissions
of SOx are to be controlled by limiting the sulphur content
of fuel oils used on board.
2.3.3 Where
the grade of fuel normally used cannot be obtained with the appropriate
fuel sulphur level, then a better grade of fuel meeting this requirement
will need to be purchased.
2.3.4 A fuel
oil management system is to detail the maximum sulphur content to
be specified when ordering fuel oils and the means adopted to verify
that the sulphur content of fuel oils supplied meets that requirement.
This management system is to include the practices to be adopted to
ensure that appropriate low sulphur fuel oils are used when the ship
is within IMO designated ‘Emission Control Areas established
for SOx and particulate matter control’ and/or the
jurisdiction of other local, national or regional ‘SOx Emission
Control regimes’ as applicable.
2.3.5 Where
testing to determine the sulphur content of fuel received on board
is to be carried out, a representative sample is to be drawn at the
time of delivery from the ship's bunker manifold using the manual
or automatic sampling methods defined in ISO 3170 or 3171, or their
national respective equivalents. Fuel sulphur content is to be subsequently
determined using the laboratory test method ISO 8754:2003 Determination
of sulphur content – Energy-dispersive X-ray fluorescence spectrometry.
2.4 Refrigeration systems
2.4.1 These requirements apply to all permanently installed refrigeration and air
conditioning installations on board with more than 3 kg of refrigerant. These
requirements do not apply to stand-alone refrigerators, freezers and ice makers used in
galleys, pantries, bars and crew accommodation.
2.4.2 The use of chlorofluorocarbons (CFC) and hydrochlorofluorocarbons (HCFCs) in
existing and new refrigeration or air conditioning installations is prohibited.
2.4.3 Where possible, natural refrigerants, such as ammonia, carbon dioxide and
hydrofluoroolefins (HFOs), should be used. Where hydrofluorocarbon (HFC) refrigerants
are used, they are to have an Ozone Depleting Potential (ODP) rating of zero and a
Global Warming Potential (GWP) of less than 1950, based on a 100- year time horizon.
2.4.4 Systems are to be arranged with suitable means of isolation so that
maintenance, servicing or repair work may be undertaken without releasing the
refrigerant charge into the atmosphere. Unavoidable minimal releases are acceptable when
using recovery units.
2.4.5 For the purposes of refrigerant recovery, the compressors are to be capable
of evacuating a system charge into a liquid receiver. Additionally, recovery units are
to be provided to evacuate a system either into the existing liquid receiver or into
cylinders dedicated for this purpose. The number of cylinders is to be sufficient to
contain the complete charge between points of isolation in the system.
2.4.6 Where different refrigerants are in use they are not to be mixed during
evacuation of systems.
2.4.7 Refrigerant leakage is to be minimised by leak prevention and periodic leak
detection procedures. The frequency of leak detection and the maximum allowable annual
leakage rate is dependent on the charge of each system and is specified in Table 11.2.1 Refrigerant leak testing - maximum
periodicity.
Table 11.2.1 Refrigerant leak testing - maximum
periodicity
Charge size
|
Periodicity
|
Leakage
|
3–30 kg
|
3 months
|
10%
|
30–300 kg
|
Monthly
|
5%
|
Over 300 kg
|
Monthly
|
<3%
|
2.4.8 Records are to be maintained demonstrating that leak testing is carried out
in accordance with the periodicity specified in Table 11.2.1 Refrigerant leak testing - maximum
periodicity by qualified personnel holding relevant
certification, using either direct or indirect measuring methods and calibrated
instruments where applicable.
2.4.9 A leak detection system appropriate to the refrigerant is to be provided to
monitor continuously the spaces into which the refrigerant could leak. An alarm is to be
activated to give warning in a permanently manned location when the concentration of
refrigerant in the space exceeds a predetermined limit, (25 ppm for ammonia; 300 ppm for
halogenated fluorocarbons). Remedial measures to repair the leakage are to be
implemented as soon as practicable after an alarm is activated. Each leak detection
system is to be checked at least once every 12 months to ensure proper functionality.
The system is to be maintained and calibrated in accordance with the manufacturer’s
recommendations and recorded in the log book.
2.4.10 Procedures for refrigerant management including adding and recovering
refrigerant charge, leak detection and the means adopted to control the loss and leakage
of refrigerants are to be established and implemented.
2.4.11 Refrigerant inventory and log book records are to be maintained
covering:
-
Refrigerant added to each system.
-
Refrigerant leaks, including remedial actions.
-
Refrigerant recovered and storage location.
-
Refrigerant disposal including quantity and location.
-
Details of personnel suitably experienced or with an applicable
qualification for maintenance of the onboard refrigerant system(s), including
relevant certification.
2.4.12 After a leak has been identified, repaired and recorded it is to be
rechecked prior to the system entering normal service. All applications, independent of
charge size, are to be checked for leakage within one month after a leak has been
repaired to ensure that the repair remains effective.
2.4.13 Records demonstrating the implementation of the operational procedures
specified in Pt 7, Ch 11, 2.4 Refrigeration systems 2.4.10, as applicable, are to be maintained. These records
are to be kept on board for a minimum period of three years, in a readily accessible
form, and are to be available for inspection by LR Surveyors, as required.
2.4.14 A refrigerant log book is to be maintained for the lifetime of the system.
It must record the quantity and type of refrigerant installed and the quantities added
and recovered during servicing, maintenance and final disposal.
2.4.15 All personnel involved in the following activities must be suitably
experienced or possess an applicable qualification:
-
installation, servicing or maintenance of the refrigeration equipment
covered by the ECO Notation;
-
checking such equipment for any leakages of refrigerant gases; or
-
repairing, or carrying out work to prevent, such leakages.
2.4.16 Flammability of Refrigerants - The Refrigerant Classification Scheme, ISO
817:2014+A1:2017, is to be considered regarding the flammability class of the
refrigerant. Where A2L and higher refrigerants are to be used in systems they are to be
designed specifically to take into account their flammability and toxicity
characteristics. These refrigerants may not replace non-flammable refrigerants when
retrofitting a system.
- Where refrigerants are classed as A2L and higher, Pt 7, Ch 11, 2.4 Refrigeration systems 2.4.4 to Pt 7, Ch 11, 2.4 Refrigeration systems 2.4.15 are applicable with the following additional
requirements:
- Spaces are to be fitted with a non sparking mechanical
ventilation system, with a capacity of at least 30 air changes per hour,
which is arranged to avoid areas where gas may accumulate, taking into
account the density of the vapour and potential ignition sources. The
ventilation system shall be separated from those serving other spaces.
- All leak detection equipment shall be suitable to use
in a hazardous area and means are to be provided to measure oxygen levels
prior to personnel entering the space.
- The leak detection is to be set to alarm at gas
concentrations above 30% lower flammable limit (LFL),
- A risk assessment reviewing the application, location
of components and the installed refrigerant charge.
- All personnel carrying out maintenance, inspections,
servicing and installation must hold an appropriate certificate for handling
such refrigerants
- All spaces containing these refrigerants are to be
indicated on a hazardous area plan.
2.5 Fire-fighting systems
2.5.1 The
use of halon or halo-carbons as the fire-extinguishing medium in fixed
fire-fighting systems or portable extinguishers is not permitted.
2.5.2 Where
foam concentrates or other chemical or liquid based fire-fighting
media with the potential to cause environmental pollution are used,
instructions and procedures are to be provided for the safe containment
and disposal of spilled media and other contaminated products during
routine maintenance and, where practicable, following emergency use.
2.6 Oil pollution prevention
2.6.3 The
oil-in-water content of the water discharged is to be less than 15
ppm. Oily bilge water is to be discharged through approved oil filtering
equipment and a 15 ppm alarm combined with a device for automatically
stopping any discharge to sea when the oil content in the discharge
exceeds 15 ppm. Full records of all discharges are to be kept.
2.6.4 The
loading or discharge connections and vent pipes/overflows associated
with fuel oils, lubricating oils, hydraulic oils and other oils are
to be fitted with drip trays. Drip trays fitted to loading or discharge
connections are to be fitted with closed drainage systems except on
tankers where alternative arrangements will be considered.
2.6.5 Fuel
oil storage, settling and service tanks are to be fitted with high
level alarms and/or acceptable overflow systems.
2.6.6 The
tank arrangement and engine room management procedures are to ensure
that any leakages and waste oil from machinery and equipment are collected
prior to disposal ashore or incineration. At all times, there is to
be sufficient capacity to store a complete lubricating oil charge
from the largest engine used for propulsion or electrical generating
purposes. The tank arrangement is to allow the lubricating oil charge
subsequently to be renovated or to be discharged ashore.
2.6.7 For
those ships which only operate on distillate fuel, the tank arrangements
in Pt 7, Ch 11, 2.6 Oil pollution prevention 2.6.6 and sludge tanks
may be combined to form a single tank. Where such a combined tank
is fitted, the total capacity is to be equal to or greater than the
aggregated total of the required individual tank capacities.
2.6.9 Discharge
piping systems to deck from the bilge holding tank, and the tank arrangements
in Pt 7, Ch 11, 2.6 Oil pollution prevention 2.6.6, are to be separate
from the fuel oil loading and transfer systems. Their piping systems
are to be terminated with the standard discharge connections specified
in MARPOL Annex I, Regulation 13.
2.6.10 Means
are to be provided for the collection and recovery of any oil spilled
on decks.
2.6.11 For
ships delivered after 1 August 2010, fuel oil tanks with a capacity
of greater than 60 m3, except overflow tanks, are to be
located in a protected location away from the ship’s side or
bottom shell plating. Tanks are to be located in accordance with the
requirements relating to fuel oil tank protection given in MARPOL
Annex I, Regulation 12A.
2.6.12 Procedures
covering the handling of all oils and oily wastes are to be established
and implemented. As a minimum, these are to cover:
-
loading, storage
and transfer of fuel oils, lubricants, hydraulic oil, thermal heating
oil and drummed oil products;
-
storage, transfer,
discharge and disposal of oily mixtures contained in the ship's sludge,
bilge holding and waste oil tanks and machinery space bilges;
-
recovery of
any oil spilled on decks.
2.7 Arrangements on ships carrying oil cargoes in bulk
2.7.1 The
constructional requirements of MARPOL Annex I, Regulations 19 and 20, as applicable, are to apply
to all oil tankers greater than 600 tonnes deadweight.
2.7.2 Cargo
tanks are to be fitted with high level alarms and/or acceptable overflow
systems.
2.7.3 The
cargo area is to have arrangements to collect accidental outflow of
oil under overfilling conditions. Accidental oil spills are to be
discharged to a slop tank or collecting tank. These tanks are not
be located in the double hull space.
2.7.4 Cargo
tank ballasting arrangements and segregated ballast systems are to
be connected to separate and distinct sea chests.
2.7.5 A non-return
valve is to be provided to isolate the cargo piping system from the
sea connections.
2.7.6 Cargo
manifold connections are to be fitted with drip trays with closed
drainage systems.
2.7.7 Cargo
manifold terminal pieces are to be designed, where practicable, in
accordance with the relevant Oil Companies International Marine Forum
(OCIMF) Recommendations for tanker manifolds and associated equipment.
2.8 Sewage treatment
2.8.2 The capacity of the sewage treatment system is to be sufficient for the
maximum number of persons on board. Treatment capacities are to be as stated in Table 11.2.2 Sewage system treatment
capacity.
Table 11.2.2 Sewage system treatment
capacity
|
Total treatment capacity in
litres/person/day
|
Black water only treated
|
Black water and grey water treated
|
Cargo
ships
|
Passenger ships
|
Conventional flushing system
|
115
|
250
|
415
|
Vacuum
flushing system
|
15
|
150
|
315
|
2.8.3 Procedures
for the operation of a sewage treatment system, including the certification
of performance, are to be established and implemented. Records are
to be maintained of maintenance, repair, remedial work and disinfectant
dosing rates.
2.8.4 The
manufacturer's restriction on materials, which may be disposed of
through the sewage treatment system, are to be clearly displayed at
each input point.
2.8.5 The
disinfectant dosing points of the sewage treatment system are to be
readily accessible. Ready access is also to be provided for the taking
of samples.
2.8.6 As
an alternative to treatment, sewage and/or grey water may be retained
on board. The sewage holding tank(s) and grey water holding tank(s)
are to be of adequate capacity, taking into account the operation
of the ship, the number of persons on board and other relevant factors
(see guidance figures in Pt 7, Ch 11, 2.8 Sewage treatment 2.8.2). The tank is to be fitted with a visual contents gauge
and a high level alarm.
2.8.9 Ventilation
pipes from the sewage system are to be independent of other vent systems.
2.8.10 A
suitable piping system from the sewage treatment system or holding
tank is to be provided to allow discharge from the system/tank to
shore reception facilities. The systems discharge pipe is to terminate
with a standard discharge connection complying with the requirements
of MARPOL Annex IV, Regulation 10 - Standard Discharge Connections.
2.8.11 Procedures
for the cleaning and safe entry of sewage treatment systems and holding
tanks, including the use of suitable personal protective equipment,
are to be provided and implemented.
2.9 VOC management
2.9.2 For
all tankers carrying crude oil, a Vapour Emission Control System is
to be fitted which has been designed and constructed in accordance
with the requirements of USCG 46, CFR 39 or the IMO Standards for
Vapour Emission Control Systems (MSC/Circular.585 – Standards for Vapour Emission Control Systems – (Adopted on 16 April 1992)). A Certificate or Statement of Compliance issued by LR
or a competent Authority recognised by LR is to be provided. As an
alternative, a self-contained Vapour Recovery System, which is of
a type approved by LR and which achieves equivalent performance to
the systems above, may be fitted.
|