Section
2 ENV characters
2.1 Anti-fouling coatings – A character
2.1.1 For
assignment of the A character, the anti-fouling system
applied to the ship’s hull is to be listed as biocide-free in
the Lloyd’s Register List of Approved Products.
2.1.2 The
following plans and documents are to be submitted:
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AFS Certificate or equivalent.
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2.2 Airborne Noise – ABN character
2.2.1 For assignment of the ABN character, the vessel’s airborne noise is to be
measured and certified in accordance with LR’s ShipRight Additional Design and
Construction Procedure for the determination of airborne noise emissions from
marine vessels. The limits are to be set by the applicant, or in accordance
with the nominated limit set within the ShipRight procedure.
2.2.2 This notation is intended to provide a measurement of the airborne noise emissions
for operation in environmentally sensitive or commercially restricted areas and is
not intended to provide a means of managing noise emissions for military
purposes.
2.3 Grey water and sewage – GW character
2.3.1 For assignment of the GW character where a plant for the treatment
of grey water is installed, the plant discharge effluent is to meet the standards
specified in Vol 3, Pt 3, Ch 2, 2.3 Grey water and sewage – GW character 2.3.4 or Vol 3, Pt 3, Ch 2, 2.3 Grey water and sewage – GW character 2.3.5, as applicable. The GW character will also be
assigned where grey water is retained on board in dedicated holding tank(s) for
discharge ashore, subject to the requirements specified in Vol 3, Pt 3, Ch 2, 2.3 Grey water and sewage – GW character 2.3.6 to Vol 3, Pt 3, Ch 2, 2.3 Grey water and sewage – GW character 2.3.10 being met.
2.3.2 The
capacity of the sewage treatment system is to be sufficient for the
maximum number of persons on board. The minimum capacity is to be
15 litres/day/person for black water and 135 litres/day/person for
grey water.
2.3.4 Where
it is not intended that the effluent be recycled or re-used for any
purpose, the effluent of the grey water treatment plant is to meet
the following standards:
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Thermotolerant
coliforms:
The geometric mean of the thermotolerant coliform count of samples
of effluent taken during a test period is not to exceed 100 thermotolerant
coliforms/100 ml as determined by membrane filter, multiple tube fermentation
or an equivalent analytical procedure.
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Total suspended
solids:
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Biochemical Oxygen
Demand (BOD5) and chemical oxygen demand (COD):
- The geometric mean of a 5-day Biochemical Oxygen Demand (BOD5)
is not to exceed 25 mg/l. The chemical oxygen demand (COD) is not
to exceed 125 mg/l. Test methods are to be ISO 15705:2002 for COD
and ISO 5815-1:2003 for carbonaceous BOD5 or other internationally
accepted equivalent test standards.
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pH: the pH of
the samples of effluent taken during the test period is to be between
6 and 8,5.
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Zero or non-detected
values: for thermotolerant coliforms, zero values are to be replaced
with a value of 1 thermotolerant coliform/100 ml to allow the calculation
of the geometric mean. For total suspended solids, BOD5 and COD values
below the limit of detection are to be replaced with one half the
limit of detection to allow the calculation of the geometric mean.
2.3.5 Where
it is intended that the effluent of the grey water treatment plant
be re-used or recycled for any purpose, the effluent is to meet the
potable water quality standards of the Naval Administration.
2.3.6 As an
alternative to treatment, where grey water is retained on board in
dedicated holding tank(s) for discharge ashore, the holding tank(s)
is to be of adequate capacity, taking into account the operation of
the ship, the number of persons on board and other relevant factors.
Each tank is to be fitted with a means to open the tank, means to
verify visually the contents of the tank and a high level alarm.
2.3.8 Ventilation
pipes from the grey water treatment system and, where provided, from
holding tank(s) are to be independent of other ventilation systems.
2.3.9 A suitable
piping system from the grey water treatment system or holding tank(s)
is to be provided to allow discharge to shore reception facilities.
The discharge pipe is to terminate with a standard discharge connection
complying with the requirements of Regulation 10 - Standard Discharge Connections. Any connection from the grey water
system to the sewage discharge is to be via a screw-down non-return
valve.
2.3.10 Records
of grey water treatment and/or discharge are to be maintained. A single
record book may be utilised for both grey water and sewage records.
Records detailing discharges from the holding tank(s) are to include:
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the date, location
and quantity of grey water discharged from the holding tank(s) either
ashore or at sea;
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rate of discharge
of untreated grey water;
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distance from
land and ship’s speed, when untreated grey water is discharged
to sea.
2.3.11 Procedures
for the cleaning and safe entry of grey water treatment systems and
holding tanks, including the use of suitable personal protective equipment,
are to be provided and implemented.
2.3.12 The
following plans and documents are to be submitted:
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Drawings showing
the grey water and sewage system arrangements;
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Treatment system
manual and documentation demonstrating that the grey water system
meets the requirements for thermotolerant coliforms, total suspended
solids, biochemical oxygen demand, chemical oxygen demand, and pH
(if treatment system fitted);
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Document showing
the grey water holding tank is of adequate capacity.
2.4 Inventory of Hazardous Materials – IHM
character
2.4.1 The IHM character will be assigned when the requirements of the Hong Kong
International Convention for the Safe and Environmentally Sound Recycling of Ships
and/or EU Ship Recycling Regulation 1257/2013, as outlined in the LR
ShipRightProcedure to obtain IHM (Inventory of Hazardous Materials)
certification, have been satisfied.
2.4.3 The ShipRight Procedure also includes procedures to be established and
implemented for the maintenance of the Inventory of Hazardous Materials throughout the
ship’s life. These maintenance procedures are to be established and implemented to
address new installations containing hazardous materials specified in Appendices 1 and 2
of the Hong Kong International Convention for the Safe and Environmentally Sound
Recycling of Ships and/or those specified in the EU Ship Recycling Regulation 1257/2013,
and relevant changes to the ship’s structure and fitted equipment.
2.4.4 In addition to the requirements of the ShipRight Procedure, where applicable,
additional Naval Administration requirements shall be considered. In such cases details
are to be provided in the tailoring document.
2.4.5 The ShipRight Procedure is intended to provide compliance with the relevant
recycling legislation for the safe and environmentally friendly recycling of ships. It
is not intended to provide procedures for the management of all substances hazardous to
human health. Separate arrangements will be required to satisfy such Naval
Administration requirements.
2.5 Monitoring, reporting and verification – MRV
character
2.5.1 For assignment of the MRV character, CO2 emissions are to be
monitored, reported and verified, in accordance with the EU Regulation 2015/757.
2.5.2 The MRV Plan is to be reviewed and CO2 emissions
independently verified by LR.
2.6 Emissions of nitrogen oxides –
NOx3 characters
2.6.1 There are no specific requirements relating to NOx emissions from boilers, incinerators
or gas turbine installations.
2.6.2 For assignment of the NOx-3 character, all installed engines with an
individual output power greater than 130 kW, other than those used solely for emergency
purposes, and associated NOx emission abatement systems are to be certified
as meeting the Tier 3 NOx emission limits specified in Regulation 13 – Nitrogen Oxides (NOx).
2.6.3 Equipment and systems used to control NOx emission levels are to:
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be arranged so that failure will not prevent continued safe operation
of the engine;
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be operated in accordance with manufacturer’s instructions;
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be designed, constructed and installed to ensure structure integrity
and freedom from significant vibration;
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be designed to include adequate hatches for inspection and
maintenance purposes; and
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be instrumented to record operation. Records of operation and the
degree of control are to be maintained.
Alternative control arrangements will be given special consideration.
2.6.4 Procedures covering the use and maintenance of the equipment and systems
used to control NOx are to be established and implemented. Records are to be
maintained which demonstrate the operation of the equipment and systems and the
resultant level of NOx emissions to the atmosphere.
2.7 Oily bilge water, OW character
2.7.1 For
assignment of the OW character, 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.
2.7.2 Fuel
oil storage, settling and service tanks are to be fitted with high
level alarms and/or acceptable overflow systems.
2.7.3 Procedures
covering the handling of all oils and oily wastes are to be established
and implemented. As a minimum, these are to cover:
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loading, storage
and transfer of fuel oils, lubricants, hydraulic oil, thermal heating
oil and drummed oil products;
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storage, transfer,
discharge and disposal of oily mixtures contained in the bilge holding
and waste oil tanks and machinery space bilges;
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recovery of any
oil spilled on decks.
2.7.4 All
drainage from machinery space bilges is to be discharged ashore, except
under exceptional circumstances.
2.7.5 Adequate
capacity for storage of oily bilge water between discharges ashore
is to be provided.
2.7.6 As an
alternative to discharging bilges ashore, discharge to sea is permitted
where it can be demonstrated that the oil-on-water content of the
water discharged is less than 5 ppm. In this case, the bilge alarm,
set at 5 ppm, is to be recalibrated or retested every five years by
the manufacturer, or other acceptable alternative, and full records
of the recalibration or retesting are to be kept on board.
2.7.7 Full
records of all oily water discharges to shore and to sea are to be
kept.
2.7.8 The
following plans and documents are to be submitted:
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Drawings showing
the arrangements of non-cargo oil loading and discharge connections,
and tank vent pipes/overflows associated with fuel oils, together
with associated drip trays and drainage systems;
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Drawings showing
the fuel oil storage, settling and service tank high level alarms/overflow
systems;
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Drawings showing
the bilge holding, waste oil and sludge tank capacities and piping
arrangements;
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Oil spill prevention
procedures including list of equipment provided for the collection
and recovery of spilled oil;
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Explanation of
the provision that has been made for storage of oily bilge water (for
ships that discharge oily water ashore);
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Type approval
certificate for the oily water separator (for ships that discharge
oily water to sea).
2.8 Oil tanks in protected locations, P character
2.8.1 For
the assignment of the P character, all fuel oil tanks,
lubricating oil tanks and hydraulic oil tanks are to be located in
a protected location away from the ship’s side or bottom shell
plating.
2.8.2 The
location of tanks is to be in accordance with the requirements relating
to fuel oil tank protection given in MARPOL
Annex I, Regulation 12A.
2.8.3 Main
engine lubricating oil drain tanks and fuel overflow tanks are excluded.
2.8.4 Arrangements
providing equivalent protection will be given special consideration.
2.8.5 Suction
wells may protrude below fuel oil tanks provided they are as small
as possible and the distance between the tank bottom and the ship’s
bottom shell plating is not reduced by more than 50 per cent.
2.8.6 The
following plans and documents are to be submitted:
- Drawings showing the arrangement of fuel oil, lubricating oil
and hydraulic oil tanks and associated suction wells.
2.9 Refrigeration systems, RS character
2.9.1 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.
2.9.2 The use of chlorofluorocarbons (CFCs) and hydrochlorofluorocarbons (HCFCs)
in existing and new refrigeration or air conditioning installations is prohibited.
2.9.3 Where possible, natural refrigerants, such as ammonia and carbon dioxide,
or 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 1000, based on a 100-year time horizon.
2.9.4 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.
2.9.5 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 to this purpose. The number of cylinders is to be sufficient to
contain the complete charge between points of isolation in the system.
2.9.6 Where different refrigerants are in use they are not to be mixed during
evacuation of systems.
2.9.7 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 2.2.1 Refrigerant leak testing - Maximum
periodicity.
Table 2.2.1 Refrigerant leak testing - Maximum
periodicity
Charge size
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Periodicity
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Leakage
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3–30 kg
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3 months
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10%
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30–300 kg
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Monthly
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5%
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Over 300 kg
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Monthly
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3%
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2.9.8 Records are to be maintained demonstrating that leak testing is carried out,
in accordance with the periodicity specified in Table 2.2.1 Refrigerant leak testing - Maximum
periodicity, by qualified personnel holding relevant
certification, using either direct or indirect measuring methods and calibrated
instruments where applicable.
2.9.9 A leak detection system in accordance with Vol 2, Pt 9, Ch 11 Gas detection, 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.
2.9.10 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.
2.9.11 Refrigerant inventory and log book records are to be maintained,
covering:
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Refrigerant added to each system.
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Refrigerant leaks, including remedial actions.
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Refrigerant recovered and storage location.
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Refrigerant disposal including quantity and location.
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Details of personnel suitably experienced or with an applicable
qualification for maintenance of the onboard refrigerant system(s), including
relevant certification.
2.9.12 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.
2.9.13 Records demonstrating the implementation of the operational procedures
specified in Vol 3, Pt 3, Ch 2, 2.9 Refrigeration systems, RS character 2.9.16, 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.
2.9.14 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.
2.9.15 All personnel involved in the following activities must be suitably
experienced or possess an applicable qualification:
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installation, servicing or maintenance of the refrigeration equipment
covered by the ENV Notation;
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checking such equipment for any leakages of refrigerant gases; or
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repairing, or carrying out work to prevent, such leakages.
2.9.16 The following plans and documents are to be submitted:
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Details and location of each permanently installed refrigeration
system. Mass of refrigerant charge in each system and the refrigerant designation
(e.g. R-134a);
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Refrigeration plant general arrangement drawing showing the number
and location of refrigerant leak detectors;
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Sample refrigerant leak testing record book;
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Refrigerant plant general arrangement drawing showing the number and
location of leak detectors;
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Operational procedure for refrigerant management including adding and
recovering refrigerant charge, leak detection and sample log book;
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Sample refrigerant inventory and log book.
2.10 Emissions of sulphur oxides, SOx
character
2.10.1 For assignment of the SOx character, all fuel used on board is to
be:
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distillate with a sulphur content not exceeding 0,10 per cent m/m;
or
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an alternative fuel or a hybrid fuel management solution which has a
resulting sulphur content which is not to exceed 0,10 per cent sulphur m/m.
2.10.2 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.
2.10.3 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.
2.10.5 The following plans and documents are to be submitted:
- Bunker specification that will be used to purchase fuel for the
ship.
2.11 Underwater noise – UWN character
2.11.1 For assignment of the UWN character, the underwater radiated noise
is to be measured and certified in accordance with LR’s ShipRight Procedure
Additional Design and Construction Procedure for the Determination of a Vessel’s
Underwater Radiated Noise. The limits are to be set by the applicant, or in
accordance with the nominated limit set within the ShipRight Procedure.
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