“ISM Code”

“ISM Code”

Mohd. Hanif Dewan, Chief Engineer  and

Maritime Lecturer & Trainer, Bangladesh.

ISM Code

-International Safety Management Code.

– ISM is made mandatory by  the chapter IX in the SOLAS from1 July 1998.

– ISM comes in to force on 1 July 2002. which is mandatory  for the wider range of cargo ships and for mobile offshore drilling units (MODUs).

Objectives:
The objectives of the ISM Code are to:
1. Ensure safety at sea;
2. Prevent human injury or loss of life; and
3. Avoid damage to the environment with focus on the marine environment and on property The ISM Code establishes the following safety management objectives of the company:
i. Provide safe practices in ship operation and working environment;
ii. Establish safeguards against all identified risks; and
iii. Continuously improve safety management skills of personnel ashore and onboard ships. These skills include the preparation for emergencies related to safety and environmental protection.

Applicable for:
The provisions of Chapter IX of the SOLAS Convention and the ISM Code apply to the following with effect from 1 July 2002:
1. All ships of 500 gross tonnage and above, engaged on international voyages and propelled by mechanical means;
2. Passenger ships engaged on international voyages;
3. The Companies (Company means the owner of the ship or any other organization or person such as the manager, or the bareboat charterer, who has assumed the responsibility for operation of the ship from the shipowner, and who on assuming such responsibility, has agreed to take over all duties and responsibility imposed by the ISM Code.)

H i s t o r y

IMO Resolution A.647 (16) – 1989.

“Guidelines on Management for the Safe Operation of Ships and for Pollution Prevention” was the first set of management guidelines for the marine industry.

IMO Resolution A.680  (17) – 1991.

Recognised the need for an appropriate organization of management to respond to the unique needs of shipboard personnel.

IMO Resolution A.741  (18) – 1993.

A shift from the IMO philosophy of hardware regulations to the software element of ship management.

Relevant Dates

Adopted into SOLAS in 1994.

Mandatory for passenger ships, including high speed craft, tankers, bulk carriers and high speed craft carrying cargo of 500 grt and over on 1st July 1998.

Mandatory for all other cargo ships, and self propelled mobile offshore drilling units of 500 grt and over on 1st July 2002.

Certification:
The application of the code will lead to the issue of two certificates:

1. The Document Of Compliance (DOC)
– will be issued to the company following a successful audit of the shore side aspects of the Safety Management System
– evidence required that the system as been in operation on at least one type of ship in the companies fleet for a period of three months.
– Specific to ship types at time of audit
– valid for 5 years
– subject to annual verification ( within 3 months of anniversary date)

  1. The Safety Management Certificate (SMC)

    – issued to each ship following audit
    – evidence that SMS has been in operation for 3 months prior to audit
    – valid DOC required
    – valid for 5 years
    – subject to one verification between the second an third anniversaries with a proviso for more frequent audits if necessary. This is more likely in the early days of ISM Code implementation.

Temporary certification
–  A 12mth valid DOC may be issued to a newly formed company or a company acquiring a new type of vessel as long as they have a SMS meeting the minimum requirements of the ISM code and can demonstrate plan for full compliance.

–  A 6 mth valid SMC may be issued to a new building or when a company takes of the responsibilities for the running of a vessel.

Safety Management System (SMS)

Safety Management objectives of the company:
1. Provide for safe working practices and a safe working environment
2. Establish safeguards against possible risks
3. Continuously improve safety management skills of personnel ashore and aboard ships,

The safety management system should ensure:

1. Compliance with mandatory rules and regulations
2. Applicable codes and guidelines both statutory and organizational are taken into account.
3. Promulgation and understanding of company and statutory regulations and guidelines. (It is the task of a visiting surveyor to test the general knowledge of company and statutory regulations and instructions)

The functional requirements for a SMS:
1. A safety and environmental policy
2. Instructions and procedures to ensure that safe operation of the vessel in compliance with relevant international and flag state legislation
3. Defined levels of authority and communication between shore and ship personnel
4. Procedures for reporting accidents and non-conformities with the code
5. Procedures for responding to emergency situations (drills etc)
6. Procedures for internal audits and management reviews
7. A system is in place for the on board generation of plans and instructions for key shipboard operations.

These tasks may be divided into two categories:

Special operations:
Those where errors only become apparent after a hazardous situation or accident has occurred. E.g. ensuring water tight integrity, navigational safety(chart corrections, passage planning), maintenance operations, bunker operations

Critical shipboard operations:
where an error will immediately cause an accident or a situation that could threaten personnel, environment or vessel. e.g. navigation in confined waters, operation in heavy weather, bunker or oil transfers, cargo operations on tankers.

ISM CODE REQUIREMENTS

Requirements

1.The ISM Code requires every Company to develop, implement and maintain a safety management system (SMS) which includes these functional requirements:

2.A safety and environmental protection policy;

3.Instructions and procedures to ensure safe operation of ships, and protection of the environment, in compliance with relevant international and flag State legislation;

4.Defined levels of authority and lines of communication between, and amongst, shore and shipboard personnel;

5.Procedures for reporting accidents and non-conformities with the provisions of this Code;

6.Procedures to prepare and respond to emergency situations; and

7.Procedures for internal audits and management reviews

PART A – IMPLEMENTATION
1.   General
2.  Safety and environmental-protection policy
3.  Company responsibilities and authority
4.  Designated person(s)
5.  Master’s responsibility and authority
6.  Resources and personnel
7.  Shipboard operations
8.  Emergency preparedness
9.  Reports and analysis of non-conformities, accidents and hazardous occurrences
10. Maintenance of the ship and equipment
11. Documentation
12. Company verification, review and evaluation

PART B – CERTIFICATION AND VERIFICATION

13. Certification and periodical verification
14. Interim certification
15. Verification
16. Forms of certificates

  1. GENERAL

    1.1   Definitions
    1.2   Objectives
    1.3   Application
    1.4   Functional requirements for a safety management system

An introduction to the general purpose of the code and its

objectives:

The purpose of the code is to provide an international standard for the safe management and operation of ships and for prevention of pollution

The objectives of the code are to ensure safety at sea, prevention of human injury or loss of life, and avoidance of damage to the environment.

  1. Safety and environmental protection policy

    – The company should establish a safety and environmental protection policy which describes how objectives listed above will be achieved.

    – The company should ensure that the policy is implemented and maintained at all levels of the organisation both ship based as well as shore based.

  2. Company responsibilities and authority

    – There must be disclosure from the owner to the administration as to who is responsible for the operation of the ship. The company should define and document responsibility, authority and interrelation of all personnel who manage, perform and verify work relating to and affecting safety and pollution prevention
    – The company must ensure there are adequate resources and shore based support for the designated person or persons to carry out their function.

  3. Designated Person(s)

    – A person or persons who has direct access to the highest levels of management providing a link between the company and those on board.

    – The responsibility and authority of the designated person is to provide for the safe operation of the vessels. He should monitor the safety and pollution prevention aspects of the operation of each vessel and ensure there are adequate shore side resources and support

  4. Master’s responsibility and authority

    – The roles and responsibilities of the Master should be clearly defined by the company with regard to the implementation of the companies policies with respect to SMS and methods for review and reporting deficiencies to the shore based management.

    – The company should ensure that the SMS operating onboard the vessel contains a clear statement emphasising the masters authority. The company should make it clear that the Master has the overall responsibility for decision making and has overriding authority with the option of adequate shore back up

  5. Resources and Personnel

    1. The company should ensure that the Master is suitably qualified and fully conversant with the SMS. They should also ensure that the ship is correctly manned.

    2. The company should ensure that there is adequate familiarisation with safety and protection of the environment for new personnel. They should ensure that the personnel has an adequate understanding of the relevant rules, regulations, guidelines and codes.

    3.Training is to be provided where necessary. Relevant information for the SMS should be promulgated and be written in an easy to understand method.

  6. Development of plans for ship board operations

    – The company should establish procedures for the generation of shipboard plans and instructions with regard to the prevention of pollution and that these should be generated by qualified personnel

  7. Emergency Preparedness:

    – The company should establish procedures for the response actions to potential emergency situations. Programmes for drill should be established and measures taken to ensure that the company’s organization can respond to hazards and accidents.

  8. Reports and analysis of non-conformities, accidents and hazardous occurrences

    – The company should ensure there is a procedure for the reporting and analysis of accidents, hazardous occurrences and non-conformities, and for the corrective action.

  9. Maintenance of the ship and equipment

    – The company is to ensure that the vessel is properly maintained. Procedures within the SMS should be in place to identify, record and plan for repair defects. A system of preventive maintenance should be in operation.
    – Regular inspections integrated with the ships operational maintenance routine should take place to ensure that the vessel is in compliance with relevant regulations.

  10. Documentation

    – The company should establish and maintain procedures for the control of all documentation relevant to the SMS. This should include;
    i. valid documents are available at all relevant locations
    ii. changes to documents are reviewed and approved to authorised personnel
    iii. obsolete documents are promptly removed
    – All documents, carried in a company approved relevant form, should be present on board

  11. Company verification, review and evaluation.

    – The company should carry out periodic audits to verify that safety and pollution prevention’s are complying with SMS. The audits and corrective actions should be carried out as per laid down procedures.
    – Personnel carrying out the audits should be independent of the areas that they are carrying out the audit unless size of the company is such that this is impractical.
    – Deficiencies or defects found should be brought to the attention of the personnel in that section and the management team so effective corrective action can be carried out

  12. Certification and Periodical Verification

    – The ship should be operated by a Company which has been issued with a DOC or with an Interim DOC. The DOC should be issued by the Administration to any Company complying with the requirements of this Code for a period specified by the Administration which should not exceed 5 years. Such a document should be accepted as evidence that the Company is capable of complying with the requirements of this Code. The DOC is only valid for the ship types explicitly indicated in the document. The validity of a DOC should be subject to annual verification by the Administration and at the request of the Administration within 3 months before or after the anniversary date.
    – A copy of the DOC should be held on board to allow the Master to produce it to the relevant authorities is required.
    – The SMC should be issued to a ship for a period which should not exceed five years by the Administration. The SMC should be issued after verifying that the Company and its shipboard management operate in accordance with the approved SMS. Such a Certificate should be accepted as evidence that the ship is complying with the requirements of this Code.

  13. Interim Certification

    – An Interim Document of Compliance may be issued to facilitate initial implementation of this Code when a Company is newly established or new ship types are to be added to an existing Document of Compliance. Such an Interim Document of Compliance should be issued for a period not exceeding 12 months by the Administration.
    –  An Interim Safety Management Certificate may be issued to new ships on delivery when a Company takes on responsibility for the operation of a ship which is new to the Company when a ship changes flag. Such an Interim Safety Management Certificate should be issued for a period not exceeding 6 months by the Administration.

  14. Verification

    – All verifications required by the provisions of this Code should be carried out in accordance with procedures acceptable to the Administration, taking into account the guidelines developed by the Organization.

  15. Forms of Certificates

    – The Document of Compliance, the Safety Management Certificate, the Interim Document of Compliance and the Interim Safety Management Certificate should be drawn up in a form corresponding to the models given in the appendix to this Code. If the language used is neither English nor French, the text should include a translation into one of these languages.

Requirements on board ship

1. Proof that the vessel is being maintained in a satisfactory condition at all times, and not only at the time of surveys-objective evidence in the form of no overdue surveys, no overdue recommendations from port or flag state inspections and that planned maintenance is being carried out and records kept.
2. Applicable codes and guidelines are being taken into consideration when operating the vessel. Vessels staff must be able to demonstrate that operations are carried out in a controlled manner utilizing information contained in these codes, guidelines and standards.
3. That emergency situations have been identified and drills are conducted to ensure the vessel and company are ready to respond to emergency situations.

Examples of the type of documentation the auditor will wish to see to verify compliance with the ISM are as follows:
1. Log books
2. Safety and management meeting minutes and follow up actions
3. Medical log
4. Company circular letters
5. Planned maintenance records
6. Records of verification
7. Records of masters review of the system
8. Records of internal audits and follow up
9. Records of chart corrections
10. Class quarterly listings
11. Records of passage planning
12. Oil record books
13. Garbage logs
14. Company manual and forms

SHIPBOARD HIGH VOLTAGE APPLICATION and SAFETIES

High Voltage in Ships

We all know about the voltages used on board a ship. It is usually a 3phase, 60Hz, 440 Volts supply being generated and distributed on board.

Every day the owners and designers aim for bigger ships for more profitability. As the ship size increases, there is a need to install more powerful engines and other machineries.

This increase in size of machineries and other equipment demands more electrical power and thus it is required to use higher voltages on board a ship.

Any Voltage used on board a ship if less than 1kV
(1000 V) then it is called as LV (Low Voltage) system and any voltage above 1kV is termed as High Voltage.
Typical Marine HV systems operate usually at 3.3kV or 6.6kV. Passenger Liners like QE2 operate at 10kV.

Defination of HV:
The numerical definition of high voltage depends on context. Two factors considered in classifying a voltage as “high voltage” are the possibility of causing a spark in air, and the danger of electric shock by contact or proximity. The definitions may refer to the voltage between two conductors of a system, or between any conductor and ground.

In electric power transmission engineering, HIGH VOLTAGE is usually considered any voltage over approximately 33,000 volts. This classification is based on the design of apparatus and insulation.
The International Electro technical Commission and its national counterparts (IET, IEEE, VDE, etc.) define high voltage as above 1000 V for alternating current, and at least 1500 V for direct current—and distinguish it from low voltage (50–1000 V AC or 120–1500 V DC) and extra-low voltage (<50 V AC or <120 V DC) circuits. This is in the context of building wiring and the safety of electrical apparatus.
– In the United States 2005 National Electrical Code (NEC), high voltage is any voltage over 600 V (article 490.2).
– British Standard BS 7671:2008 defines high voltage as any voltage difference between conductors that is higher than 1000 V AC or 1500 V ripple-free DC, or any voltage difference between a conductor and Earth that is higher than 600 V AC or 900 V ripple-free DC.

WHAT IS CLASSED AS HIGH VOLTAGE?
In marine practice,
– voltages below 1,000Vac (1kV) are considered low voltage, and
– high voltage is any voltage above 1kV. Typical marine high voltage system voltages are 3.3kV, 6.6kV and 11kV.

THE MAJOR DIFFERENCES BETWEEN HIGH VOLTAGE SUPPLY AND LOW VOLTAGE SUPPLY ON BOARD SHIPS ARE:
1. H
igh voltage systems are more extensive with complex networks and connections,
2. Isolated equipment MUST BE earthed down
3. Access to high voltage areas should be strictly limited and controlled
4. Isolation procedures are more involved
5. Switching strategies should be formulated and recorded
6. Specific high voltage test probes and instruments must be used
7. Diagnostic insulation resistance testing is necessary
8. High voltage systems are usually earthed neutral and use current limiting resistors
9. Special high voltage circuit breakers have to be installed
Why High Voltage in Ships?

– Higher power requirements on board vessels is the foremost reason for the evolution of HV in ships.
– Higher power requirements have been necessitated by development of larger vessels required for container transport particularly reefer containers.
– Gas carriers needing extensive cargo cooling Electrical Propulsion.
– For ships with a large electrical power demand it is necessary to utilise the benefits of a high voltage (HV) installation.

– The design benefits relate to the simple ohms law relationship that current (for a given power) is reduced as the voltage is increased. Working at high voltage significantly reduces the relative overall size and weight of electrical power equipment.

AS PER OHMS LAW
POWER = VOLTAGE  x CURRENT
For a given Power,
Higher the Voltage, Lesser  is the Current
440 KW = 440,000 Watts
=  440  Volts    x    1000 Amps
=1100  Volts     x      400 Amps
=11000  Volts    x       40 Amps

– When large loads are connected to the LV system the magnitude of current flow becomes too large resulting in overheating due to high iron and copper losses.
P = VI CosФ
Copper loss =I² R [kW]
HV levels of 3.3 kV, 6.6 kV and 11 kV are regularly employed ashore for regional power distribution and industrial motor drives.

For example, a motor (let us assume a bow thruster), may be of a smaller size if it designed to operate on 6600 Volts.
For the same power, the motor would be of a smaller size if it is designed for 6600Volts when compared to 440Volts.

Thus these are the major reasons why recent ships have shifted towards high voltage systems.

The main disadvantage perceived by the user /maintainer, when working in an HV installation, is the very necessary adherence to stringent safety procedures.
Advantages/Disadvantages of using HV Advantages:

Advantages:
For a given power, Higher voltage means Lower current, resulting in:
– Reduction in size of generators, motors, cables etc.
– Saving of Space and weight
– Ease of Installation
– Reduction in cost of Installation
– Lower losses – more efficient utilization of generated  power
– Reduction in short circuit levels in the system which decides the design and application of the electrical equipment used in the power system.

Disadvantages:

1. Higher Insulation Requirements for cables and equipment used in the system.
2. Higher risk factor and the necessity for strict adherence to stringent safety procedures.

Marine Electrical System

– Some installations may feed the ships sub stations directly with HV and step- down to 440 V locally.

– The PEM drives in this example are synchronous motors which require a controlled low voltage excitation supply current to magnetise the rotor poles.
– This supply is obtained from the HV switchboard via a step-down transformer but an alternative arrangement would be to obtain the excitation supply from the 440 V ER sub switchboard.

  • Hazardous Electrical Voltage Training ChecklistThe training requirements below apply to all employees who face a risk of electrical shock that is not reduced to a safe level by electrical installation requirements and
    who must work on or near energized components.

    All Qualified High Voltage Electrical Workers who work on high voltage equipment (> 600 volts) are required
    to be trained on safety-related work practices that pertain to their jobs and in the following topics below:

    The skills and techniques necessary to distinguish exposed live parts from other parts of electrical equipment.
    • The skills and techniques necessary to determine the nominal voltage of exposed live parts.

  • The clearance distances and the corresponding voltage to which the Qualified Person will be exposed.
    • Safely de-energizing of parts and subsequent electrical lockout and tagging procedures as required by the electrical standard.
    • Proper precautionary work techniques.
    • Proper use of PPE to include non-conductive gloves, aprons, head protection, safety glasses, and face shields.
  • Proper selection and use of rated test instruments and equipment, including the capability to visually inspect all parts of the test equipment for defects.
    • Use of insulating and shielding materials for employee protection to include auxiliary shields, guards, mats, or other specific equipment.
    • Proper use of insulated tools or other non-conductive devices such as fuse pullers, fish tapes, hot sticks, ropes, or handlines.
    • The importance of illumination and to work only in properly illuminated areas.
  • Proper work techniques for work in enclosed or confined work spaces.
    • Removal or special handing of any conductive materials and equipment.
    • Proper and safe use of portable ladders around electrical equipment.
    • Removal of any conductive jewelry or apparel.
    • Proper alerting techniques such as using safety signs and tags, barricades,attendants, and work practices.
    • Any other safety related work practice not listed above but necessary for them to safely do their job

Electric Shock:
Voltages greater than 50 v applied across dry unbroken human skin can cause heart fibrillation if they produce electric currents in body tissues that happen to pass through the chest area.
Accidental contact with high voltage supplying sufficient energy may result in severe injury or death. This can occur as a person’s body provides a path for current flow, causing tissue damage and heart failure. Other injuries can include burns from the arc generated by the accidental contact. These burns can be especially dangerous if the victim’s airways are affected.

 

Hazards of High Voltage

Arcing:
An unintentional electric arc occurs during opening of a breaker, contactor or switch, when the circuit tries to maintain itself in the form of an arc.
During an insulation failure, when current flows to ground or any other short circuit path in the form of accidental tool slipping between conducting surfaces, causing a short circuit.
Results of an electric arc:
Temperatures at the arc terminals can reach or exceed 35,000° f or 20,000˚c or four times the temperature of sun’s surface. The heat and intense light at the point of arc is called the arc flash.
Air surrounding the arc is instantly heated and the conductors are vaporised causing a pressure wave termed as ARC BLAST.

Hazards of an Arc Flash:
– During an arc flash, sudden release of large amounts of heat and light energy takes place at the point of arc.
– Exposure frequently results in a variety of serious injuries and may even be fatal, even when the worker is ten feet or more from the arc center.
– Equipments can suffer permanent damage.
– Nearby inflammable materials may be ignited resulting in secondary fires.

Hazards of Arc Blasts & ejected materials:
– An arc flash may be accompanied by an arc blast
– The arc blast causes equipment to literally explode ejecting parts with life threatening force. – Heated and vaporised conducting materials surrounding the arc expand rapidly causing effects comparable to an explosive charge.
– They may project molten particles causing eye injuries. The sound that ensues can harm the hearing.

  • Potential injuries:
    – At some distance from the arc, temperatures are often high enough to instantly destroy skin and tissue. Skin temperatures above 100˚C ( about 210˚F) for 0.1sec result in irreversible tissue damage, defined as an incurable burn.
    – Heated air and molten materials from arc faults cause ordinary clothing to burst into flames even if not directly in contact with the arc. Synthetic fibers may melt and adhere to the skin resulting in secondary burns.
    – Even when safety goggles are worn, arc flash may cause severe damage to vision and or blindness. Intense UV light created by arc flash can damage the retina. Pressure created from arc blasts can also compress the eye, severely damaging vision.
    – Hearing can also be affected by the loud noise and extreme pressure changes created by arc blasts. Sound blasts with arc blasts exceed 140dB which is equal to an airplane taking off. Sudden pressure changes exceeding 720lbs/sq.ft for 400ms can also rupture eardrums. Even at lesser pressure, serious or permanent damage to hearing may occur.

Short Circuit

A short circuit ( or a fault ) is said to have taken place when the current is not confined to its normal path of flow but diverted through alternate path(s).

– During short circuit, the current rises much above the normal value.
– Short circuit level is the maximum possible current that flows at the point of fault during a short circuit.

Effects of short circuit:
High currents during Short circuits can cause damage to electrical installation by giving rise to excessive
Thermal Stresses, Mechanical Stresses , Arcing.

Methods adopted to prevent effects of short circuit in a system:

– A well-designed Protective Relay system trips out a breaker(s) and isolates the faulty circuit from the power source within a short time to prevent/minimise effects of high short circuit current, as and when it occurs.
– The equipment in the system, the cables, the switchgear, the busbar, the generators are designed to withstand the effects of short circuit during that short period.

Calculation  of the short circuit levels in the system is therefore required to help in:
a. Designing an appropriate Protective Relay System
b. Choosing the right switchgear with suitable short circuit withstand capacity to be used in the system.

High Voltage Safety and Precautions

Making personal contact with any electric voltage is potentially dangerous. At high voltage (>1000 V) levels the electric shock potential is lethal. Body resistance decreases with increased voltage level which enhances the current flow. Remember that an electric shock current as low as 15 mA can be fatal. So,the risk to people working in HV areas is greatly minimised by the diligent application of sensible general and company safety regulations and procedures.

Personnel who are required to routinely test and maintain HV equipment should be trained in the necessary practical safety procedures and certified as qualified for this duty.

Approved safety clothing, footwear, eye protection and hard hat should be used where danger may arise from arcs, hot surfaces and high voltage etc.

Safety equipment should be used by electrical workers includes insulated rubber gloves and mats. These protect the user from electric shock.

Safety equipment is tested regularly to ensure it is still protecting the user. Testing companies can test at up 300,000 volts and offer services from glove testing to Elevated Working Platform or EWP Truck testing.

 A insulated material or rubber mat can be used as a dead front of all electrical installations and equipments.

The access to HV switchboards and equipment must be strictly controlled by using a permit-to-work scheme and isolation procedures together with live-line tests and earthing-down before any work is started. The electrical permit requirements and procedures are similar to permits used to control access in any hot-work situation, e.g. welding, cutting, burning etc. in a potentially hazardous area.

HIGH VOLTAGE SAFETY RULES AND PROCEDURES

All safety rules presented in this document are intended to ensure safe working conditions while working with potentially dangerous voltages. It is assumed that all personnel working with potentially dangerous voltages have been trained in basic electrical safety procedures.

 1. This guidance does not apply where equipment has been isolated, discharged, disconnected and removed from the system or installation.
2. Equipment that is considered by an Authorised Person (HV) to be in a dangerous condition should be isolated elsewhere and action taken to prevent it from being reconnected to the electricity supply.
3. All working on, or testing of, high voltage equipment connected to a system should be authorised by a permit-to-work or a sanction-for- test following the procedures as described in Practical Exercises no. 4
4. No hand or tool (unless the tool has been designed for the purpose) must make contact with any high voltage conductor unless that conductor has been confirmed dead by an Authorised Person (HV) in the presence of the Competent Person (HV).
5. Where any work or test requires an Accompanying Safety Person (HV) to be present, he/she should be appointed before that work or testing can begin.
6. Voltage test indicators should be tested immediately before and after use against a test supply designed for the purpose.
7. Where the procedures involve the application of circuit main earths, the unauthorised removal of such earths should be prevented, wherever practicable, by the application of safety locks.
8. Where the procedures involve the removal of circuit main earths, that is, testing under a sanction-for-test, the earths will be secured with working locks. The keys to these locks will be
retained by the Duty Authorised Person (HV), who will remove and replace the earths as requested.

Precaution prior to live voltage and phasing checks:

1. Where live phasing is to be undertaken, the area containing exposed live conductors should be regarded as a high voltage test enclosure.
2. Approved equipment used for live voltage and phasing checking at high voltage should be tested immediately before and after use against a high voltage test supply.
3. Live voltage and phase checking on high voltage equipment may only be undertaken by a Authorised Person (HV), with assistance if necessary from a Competent Person (HV)
acting on verbal instructions from the Authorised Person (HV). Neither a permit-to-work nor a sanction-for-test is required, but the Authorised Person (HV) and any assistant should
be accompanied by an Accompanying Safety Person
(HV).

Testing at high voltage:
1. Where high voltage tests are to be undertaken, a sanction-for-test should be issued to the Competent Person (HV) who is to be present throughout the duration of the tests.
2. The areas containing exposed live conductors, test equipment and any high voltage test connection should be regarded as high voltage enclosures.

High voltage test enclosures:
1. Unauthorised access to a high voltage test enclosure should be prevented by, as a minimum, red and white striped tape not less than 25 mm wide, suspended on posts, and by the display of high voltage danger signs. An Accompanying Safety Person (HV) or the Duty Authorised Person (HV) should be present throughout the duration of the tests, and the area should be continually watched while testing is in progress.

Work on busbar spouts of multi-panel switchboards

When work is to be carried out on busbar spouts, the following operations should be carried out in strict sequence:

a.  the Authorised Person (HV) should record
the details of necessary safety precautions  and switching operations on a safety programme and produce an isolation and earthing diagram;
b.  the section of the busbar spouts on which work is to be carried out must be isolated from all points of supply from which it can be made live;
c.  the isolating arrangements should be locked so that they cannot be operated, and shutters of live spouts locked shut. Caution signs should be fixed to the isolating points;
d.  where applicable, danger signs should be attached on or adjacent to the live electrical equipment at the limits of the zone in which work is to be carried out;

  1. busbars should be checked by means of an approved voltage indicator to verify that they are dead, the indicator itself being tested immediately before and after use. The checking with the voltage indicator should be done on the panel to which the circuit main earths are to be applied. This test should also be made on the panel on which the work is carried out;
    f. circuit main earths should be applied at a panel on the isolated section of the busbar other than that at which work is to be done using the method recommended by the switchgear manufacturers. The insertion of hands or any tool into the contact spouts for this purpose is not an acceptable practice;
    g.  an earth connection should also be applied to all phases at the point-of-work;
    h.  the permit-to-work should be issued to cover the work to be done. During the course of the work, where applicable, the earth connection(s) at the point-of-work may be removed one phase at a time. Each phase earth connection must be replaced before a second-phase earth connection is removed;
    j.   on completion of the work, the permit-to-work should be cancelled.

Definition of safety terms:

Definitions presented here are those deemed necessary and suitable for electrical laboratory applications present in the Electronics and Electrical Engineering Laboratory. They should not be assumed to be directly related to definitions presented in other electrical standards or codes.

High Voltage: Any voltage exceeding 1000 V rms or 1000 V dc with current capability exceeding 2 mA ac or 3 mA dc, or for an impulse voltage generator having a stored energy in excess of 10 mJ. These current and energy levels are slightly below the startle response threshold.

Moderate Voltage: Any voltage exceeding 120 V rms (nominal power line voltage) or 120 V dc, but not exceeding 1000 V (rms or dc), with a current capability exceeding 2 mA ac or 3 mA dc.

Temporary Setups: Systems set up for measurements over a time period not exceeding three months.

Test Area: Area in which moderate voltages are accessible, and which has been clearly delineated by fences, ropes, and barriers.

Troubleshooting: Procedure during which energized  bare connectors  at  moderate or high voltages might be temporarily exposed for the purpose of repair or problem diagnosis.

Inter lock: A safety circuit designed to prevent energizing high- or moderate-voltage power supplies until all access doors are closed, and to immediately de-energize such power supplies if the door is opened. Note that this function does not necessarily ensure full discharge of stored energy.

Bare Conductor: A conductor having no covering or electrical insulation whatsoever.

Covered Conductor : A conductor enclosed within a material of composition or thickness not defined as electrical insulation .

Insulated Conductor: A conductor encased within material of composition and thickness defined as electrical insulation.

Exposed Conductor: Capable of being inadvertently touched or approached nearer than a safe distance by a person. It applies to parts that are not suitably guarded, isolated, or insulated.

Unattended Operation: The operation of a permanent setup for electrical measurements  for a time period longer than can be reasonably attended by staff.

Enclosed: Surrounded by a case, housing, fence or wall(s) that prevents persons from accidentally contacting energized parts.

Temporary Setups

When troubleshooting a setup with exposed or bare conductors at high or moderate voltages, it may be necessary to temporarily bypass safety interlocks. Such procedures may only be performed under two-person operating conditions.
In instances where troubleshooting a system or particular equipment becomes frequent (at least once every six months) Group Leader approval is required. In all cases two staff members must be present when high voltage is energized and the interlock(s) bypassed. When troubleshooting a single piece of equipment in such a way that personnel may have access to high or moderate voltage (for example, repairing an instrument), two persons should be present.
The “keep one hand in the pocket” rule is strongly encouraged.

Signs and Warning Lights

DANGER HIGH VOLTAGE signs must be on display on all entrances to all test areas where bare conductors are present at both moderate and high voltages. These signs should be in the vicinity of the test area and on the outside of the door leading to the laboratory area.
A warning light, preferably flashing, must be on when high or moderate voltages are present, and ideally should be activated by the energizing of the apparatus. The warning light must be clearly visible from the area surrounding the test area. In special cases where such a light interferes with an experiment, it can be omitted with special permission from the Group Leader and Division Chief.

In all cases where there is direct access from the outside hallway to the area where high or moderate voltages are present, a warning light, DANGER HIGH VOLTAGE sign, a safety interlock (for high voltages) and a locked door are required.
For unattended setups with bare conductors at high or moderate voltage, a warning sign with the names of two contact persons and the dates of unattended operation must be posted on the door leading to the high-voltage area. In addition, written notice of unattended testing of high or moderate voltage with bare conductors must be sent to the NIST Fire Department (in Gaithersburg) or to the Engineering, Safety, and Support Division (in Boulder) clearly stating the anticipated dates of operation. A warning light on or near the door to the laboratory must be illuminated when high or moderate voltages with bare conductors are present.

Grounding Stick

Before touching a high-voltage circuit or before leaving it unattended and exposed, it must be de-energized and grounded with a grounding stick. The grounding stick must be left on the high-voltage terminal until the circuit is about to be re-energized. Grounding sticks must be available near entrances to high-voltage areas. Automatic grounding arrangements or systems that employ audible warning tones to remind personnel to ground the high-voltage equipment are strongly encouraged for two-person operation, and are mandatory for one-person or unattended operation.
For systems with bare conductors at moderate voltages, the use of a grounding stick is strongly recommended, particularly if the setup contains energy-storage devices.

Modes of Operation
 Two-person: Two-person operation is the normal mode of operation where high or moderated voltages are present. Allowed exceptions are:

When all potentially dangerous voltages are confined inside a grounded or insulated box, or where the voltages are constrained in a shielded cable, or where the is no access to bare conductors
When one-person or unattended operation setups have been designed and approved according to the rules set out in this document and with appropriate approval.
It is presumed that both individuals participating in two-person operation will follow basic high-voltage safety procedures and will monitor each other’s actions to ensure safe behavior.

One-person: One-person operation of systems using high and moderate voltages with bare or exposed conductors, may be approved, after appropriate review and authorization, in order to provide for the efficient use of staff for long-term applications where it is judged that safety would not be compromised.

Unattended: It is recognized that in order to run efficient calibration services and maintain appropriate delivery schedules, unattended operation of systems using high and moderate voltages may be necessary. In such cases, unattended operation is permitted.

with appropriate review and authorization, for systems having no bare or exposed conductors, and where required warning signs, lights, and barriers are present.

Unattended operation of setups with bare or exposed conductors at high and moderate voltages may be necessary under special circumstances, such as for unusually long data- acquisition periods. This is meant to be a rare occurrence. Should this mode of operation be frequently employed, then the apparatus should be modified to enclose all potentially dangerous voltages.

Circuit Breakers & Disconnects

Circuit breakers, disconnects or contactors used to energize a high-voltage source must be left in an open position when the supply is not in use. Laboratories should always be left in a configuration that at least two switches must be used to energize high-voltage circuits. Whenever possible a “return-to-zero-before energizing” interlock should be incorporated into the high-voltage supply.

Proper Circuit Design Recommendations
– Draw the circuit and study it before wiring it for operation at high voltage.
– Make sure all devices that require grounding are securely grounded.
– Allow adequate clearances between high-voltage terminals and ground.
– Solicit a second opinion before operation for the first time.

Transformers and Variacs:
– Make certain that one terminal of each transformer winding used to provide a separately derived system (this excludes the winding connected to the power supply) as well as the transformer or Variac case are properly grounded.
– The common terminal of a Variac should be connected to the supply neutral.
– Cascade transformers and, in some cases, isolation transformers are exceptions.

  • General Information PERMIT-T0-WORK:– Issued by an authorised person to a responsible person who will perform the task of repair/maintenance.
    – Generally valid only for 24-Hrs. Permit to be re-validated by the permit-holder if work extends beyond 24 Hrs. after issue Formats will vary and be customized for a particular vessel/marine installation.

Permit To Work- BROAD GUIDELINES:

Prepared in duplicate copy and has at least five sections:

– 1st section states the nature of work to be carried out.
– 2nd section declares where electrical isolation and earthing have been applied and where Danger /Caution notices have been displayed.
– 3rd section is signed by the Person receiving the Permit acknowledging that he is satisfied with the safety precautions taken and the Isolation/ Earthing measures adopted.
– 4th section is signed by the Permit-holder that the work has been completed/suspended.
– 5th Section is signed by the Issuing authority cancelling the Permit.

High Voltage Safety and Precautions

For the purposes of safety, HV equipment includes the LV field system for a propulsion motor as it is an integrated part of the overall HV equipment. From the HV generators, the network supplies HV motors (for propulsion, side thrusters and air conditioning compressors) and the main transformer feeders to the 440 V switchboard. Further distribution links are made to interconnect with the emergency switchboard.

HV Circuit breakers and contactors

Probably the main difference between a HV and an LV system occurs at the HV main switchboard. For HV, the circuit breaker types may be air-break, oil-break, gas-break using SF6 (sulphur hexafluoride) or vacuum-break. Of these types, the most popular and reliable are the vacuum interrupters, which may also be used as contactors in HV motor starters.

Each phase of a vacuum circuit breaker or contactor consists of a fixed and moving contact within a sealed, evacuated envelope of borosilicate glass. The moving contact is operated via flexible metal bellows by a charging motor/spring or solenoid operating mechanism. The high electric strength of a vacuum allows a very short contact separation, and a rapid restrike-free interruption of the arc is achieved.

When an alternating current is interrupted by the separating contacts, an arc is formed by a metal vapour from the material on the contact surfaces and this continues to flow until a current zero is approached in the a.c. wave form. At this instant the arc is replaced by a region of high dielectric strength which is capable of withstanding a high recovery voltage. Most of the metal vapour condenses back on to the contacts and is available for subsequent arcing. A small amount is deposited on the shield placed around the contacts which protects the insulation of the enclosure. As the arcing period is very short (typically about 15 ms), the arc energy is very much lower than that in air-break circuit-breakers so vacuum contacts suffer considerably less wear.

Because of its very short contact travel a vacuum interrupter has the following advantages:

– compact quiet unit

– minimum maintenance

– non-flammable and non-toxic

– The life of the unit is governed by contact erosion but could be up to 20 years.

In the gas-type circuit breaker, the contacts are separated in an SF6 (sulphur hexafluoride) gas which is typically at a sealed pressure chamber at 500 kPa or 5 bar (when tested at 20° C).
HV Insulation Requirements

The HV winding arrangements for generators, transformers and motors are similar to those at LV except for the need for better insulating materials such as Micalastic or similar.

The HV windings for transformers are generally insulated with an epoxy resin/powdered quartz compound. This is a non-hazardous material which is maintenance free, humidity resistant and tropicalised.

Conductor insulation for an HV cable requires a more complicated design than is necessary for an LV type. However, less copper area is required for HV conductors which allows a significant saving in space and weight for an easier cable installation. Where the insulation is air (e.g. between bare-metal live parts and earth within switchboards and in terminal boxes) greater clearance and creepage distances are necessary in HV equipment.

INSULATION RESISTANCE TESTS OF HV EQUIPMENT:

– A 5000 Vdc Megger, Hand-cranking or Electronic can be used for equipments upto 6.6KV.

– For routine testing of IR, 5000 Vdc must be applied for 1 minute  either by cranking at constant speed with a Hand-cranking megger or by maintaining a 5000 Vdc continuously by a PB in an Electronic Megger.

IR values taken at different temperatures are unreliable, particularly if the temperature differences are more than 10°C.

SAFETIES OF IR TEST TO HV EQUIPMENTS

1. Before applying an IR test to HV equipment its power supply must be switched off, isolated, confirmed dead by an approved live-line tester and then earthed for complete safety.
2. The correct procedure is to connect the IR tester to the circuit under test with the safety earth connection ON. The safety earth may be applied through a switch connection at the supply circuit breaker or by a temporary earth connection local to the test point. This is to ensure that the operator never touches a unearthed conductor.
3. With the IR tester now connected, the safety earth is disconnected (using an insulated extension tool for the temporary earth). Now the IR test is applied and recorded. The safety earth is now reconnected  before the IR tester is disconnected.

This safety routine must be applied for each separate  IR test.

At prescribed intervals and particularly after a major repair work on an equipment or switchgear, a Polarisation Index(PI) may be taken to assess the condition of insulation of the equipment. PI readings are less sensitive to temperature changes.

POLARISATION INDEX ( PI ):

When the routine IR value tests (taken at different temperatures) are doubtful or during annual refit or after major repairs are undertaken, a PI test is conducted.

– PI value is the ratio between the IR value recorded  after application of the test voltage continuously for 10 minutes to the value recorded after 1 minute of application.
– PI value= 2.0 or more is considered satisfactory.

A motor-driven megger is essential for carrying out a PI test.

High Voltage Equipment Testing

The high voltage (e.g. 6.6 kV) installation covers the generation, main supply cables, switchgear, transformers, electric propulsion (if fitted) and a few large motors e.g. for side-thrusters and air conditioning compressors. For all electrical equipment the key indicator to its safety and general condition is its insulation resistance (IR) and this is particularly so for HV apparatus. The IR must be tested periodically between phases and between phases and earth. HV equipment that is well designed and maintained, operated within its power and temperature ratings should have a useful insulation life of 20 years.

Large currents flowing through machine windings, cables, bus-bars and main circuit breaker contacts will cause a temperature rise due to I2R resistive heating. Where overheating is suspected, e.g. at a bolted bus-bar joint in the main switchboard, the local continuity resistance may be measured and checked against the manufacturers recommendations or compared with similar equipment that is known to be satisfactory.

A normal ohmmeter is not suitable as it will only drive a few mA through the test circuit. A special low resistance tester or micro-ohmmeter (traditionally called a ducter) must be used which drives a calibrated current (usually I = 10 A) through the circuit while measuring the volt-drop (V) across the circuit. The meter calculates R from V/I and displays the test result. For a healthy bus-bar joint a continuity of a few mΩ would be expected.

Normally the safe testing of HV equipment requires that it is disconnected from its power supply. Unfortunately, it is very difficult, impossible and unsafe to closely observe the on-load operation of internal components within HV enclosures. This is partly resolved by temperature measurement with an recording infra-red camera from a safe distance. The camera is used to scan an area and the recorded infra-red image is then processed by a computer program to display hot-spots and a thermal profile across the equipment.

Safety testing of HV equipment:

Normally the safe testing of HV equipment requires that it is disconnected from its power supply. Unfortunately, it is very difficult, impossible and unsafe to closely observe the on-load operation of internal components within HV enclosures. This is partly resolved by temperature measurement with an recording infra-red camera from a safe distance. The camera is used to scan an area and the recorded infra-red image is then processed by a computer program to display hot-spots and a thermal profile across the equipment.

SANCTION-FOR-TEST SYSTEM
– following work on a high voltage system, it is often necessary to perform various tests. testing should only be carried out after the circuit main earth (CME) has been removed.
– a sanction-for-test declaration should be issued in an identical manner to a permit to work provided and it should not be issued on any apparatus where a permit to work or where another sanction-fortest is in force.
Note That:
A sanction-for-test is not a permit to work.
An example of a sanction-for-test declaration is shown in the code of safe working practices (COSWP) 2010 edition annex 16.2.1.

Additional Procedures Needed for HV systems

Limitation of access form

When carrying out high voltage maintenance, it may be dangerous to allow anyone to work adjacent to high voltage equipment, as workers may not be familiar with the risks involved when working on or nearby high voltage equipment. The limitation of access form states the type of work that is allowed near high voltage equipment and safety precautions. the form is issued and signed by the chief engineer AND electrical officer, and countersigned by the persons carrying out
the work.

Additional Procedures Needed for HV systems

Earthing Down

Earthing down is a very important concept to understand when
working with high voltage systems. It is important to ensure that any stored electrical energy in equipment insulation after isolation is safely discharged to earth. the higher levels of insulation resistance required on high voltage cabling leads to higher values of insulation capacitance (c) and greater stored energy (w). this is demonstrated by the electrical formula:
energy stored (w) joules = (capacitance x voltage²)/2

Earthing down ensures that isolated equipment remains safe. Additional Procedures Needed for HV systems

There are two types of earthing down a high voltage switchboard:

1. CIRCUIT EARTHING
– an incoming or outgoing feeder cable is connected by a heavy earth connection from earth to all three
conductors after the circuit breaker has been racked out. This is done at the circuit breaker using a special key. This key is then locked in the key safe. The circuit breaker cannot be racked in until the circuit earth has been removed.

2. BUSBAR EARTHING
– when it is necessary to work on a section of the
busbars, they must be completely isolated from all possible electrical sources. This will include generator incoming cables, section or bus-tie breakers, and transformers on that busbar section. The busbars are connected together and earthed down using portable leads, which give visible confirmation of the earthing arrangement.

High voltage safety checklists for the following can be found in onboard “Company Safety Manual” and sample can be found in the “Code of Safe working Practices for Merchant Seaman (COSWP)” 2010 edition:
• working on high voltage equipment/installations
• switchgear operation
• withdrawn apparatus not being used
• locking off
• insulation testing
• supply failure
• entry to high voltage enclosures
• earthing
• working on high voltage cables
• working on transformers
• safety signs
• correct personal protective equipment

Personnel should not work on High Voltage equipment unless it is dead, isolated and earthed at all high voltage disconnection points. The area should be secured, permits to work or sanction for test notices issued, access should be limited and only competent personnel should witness the testing to prove isolation.
Work Procedures in High Voltage
Working procedures are divided in to three distinct groups.
1. Dead working
2. Live working
3. Working in the vicinity of live parts

Dead Working:
Work activity on electrical installations which are neither live nor charged, carried out after taking all measures to prevent electrical danger.

Precautions before starting work
– Obtain PTW/Sanction- to-Test Permit before commencing work
– Test and prove that the equipment is DEAD before earthing. (with a HV line tester)
– Earth the equipment

Working in the vicinity of live parts:

– All work activity in which the worker enters the vicinity of live zone with his body or with tools and equipment without encroaching in to live zone.

– Using the correct personal protective equipment (PPE) and following safe work practices will minimize risk of electrical shock hazards

HIGH VOLTAGE EQUIPMENT
A typical high voltage installation will incorporate only high voltage rated equipment on the following:

1. Generating sets
2. High voltage switchboards with associated switchgear, protection devices and instrumentation
high voltage cables
3. high voltage/low voltage step-down transformers to service low voltage consumers
4. high voltage/high voltage (typically 6.6kV/2.9kV) step-down transformers supplying propulsion converters and motors
5. high voltage motors for propulsion, thrusters, air conditioning and compressors

A high voltage electrical shock is a significant danger to any person carrying out electrical work. Any simultaneous contact with a part of the body and a live conductor will probably result in a fatal electric shock. There is also a risk of severe burn injuries from arcing if conductors are accidentally short-circuited.
A high voltage electric shock will almost certainly lead to severe injury or a fatality.
Factors that could increase the risk of receiving an electric shock:
1. High voltage work may be carried out close to a person that is not familiar with high voltage hazards. therefore, the area must be secured from the surrounding non-electrical work and danger notices posted.
2. Areas of earthed metal that can be easily touched increase the possibility of electric shock from a high voltage conductor.

Dangers Working With High Voltage Equipments

  1. High voltage insulation testing (flash testing) can be particularly hazardous when several parts of the equipment are energised for a period of time.
    4. Equipment using water as part of the high voltage plant can lead to an increased risk of injury.
    5. Using test instruments when taking high voltage measurements can increase the risk of injury if the protective earth conductor is not connected. This can result in the enclosure of the instrument becoming live at dangerous voltages.
    6. High voltage equipment will store energy after disconnection. for example, on a 6.6kv switchboard, a fatal residual capacitive charge may still be present hours or even days later.
    7. if, during maintenance, a high voltage circuit main earth is removed from the system, it must not be worked on as the high voltage cabling can recharge itself to a high voltage (3–5kv).

Dangers Working With High Voltage Equipments

TRANSFORMER TESTING & MAINTENANCE

What is a transformer?

Transformer is a static device which transforms a.c. electrical power from one voltage to another voltage keeping the frequency same by electromagnetic induction.

Main features of transformer:

Outdoor,oil cooled, 3 phase,50hz

Primary is delta  connected and secondary is star connected.

Naturaly cooled

Amongst all the types of transformers this is the most required and most used type.

Parts of transformer:

  • MAIN TANK
  • RADIATORS
  • CONSERVATOR
  • EXPLOSION VENT
  • LIFTING LUGS
  • AIR RELEASE PLUG
  • OIL LEVEL INDICATOR
  • TAP CHANGER
  • WHEELS
  • HV/LV BUSHINGS
  • FILTER VALVES
  • OIL FILLING PLUG
  • DRAIN PLUG
  • CABLE BOX

TESTING OF TRANSFORMER:

  • Testing is carried out as per PMS or Company checklist.
  • Routine , type tests & special tests
  • Routine tests ( to be carried out on each job):
  1. Measurement of winding resistance
  2. Measurement of insulation resistance
  3. Seperate source voltage withstand test

(high voltage tests on HV & LV)

4.Induced over voltage withstand test (dvdf test)

5.Measurement of voltage ratio

6.Measurement of no load loss & current.

7.Measurement of load loss & impedence.(efficiency & regulation)

8.Vector group verification

9.Oil bdv test.

10.Tests on oltc (if attached)

MAINTENANCE OF TRANSFORMER

– Transformer is the heart of any power system. Hence preventive maintenance is always cost effective and time saving. Any failure to the transformer can extremely affect the whole functioning of the organization.

MAINTENANCE PROCEDURE

OIL :

  1. Oil level checking. Leakages to be attended.
  2. Oil BDV & acidity checking at regular intervals. If acidity is between 0.5 to 1mg KOH, oil should be kept under observation.
  3. BDV, Color and smell of oil are indicative.
  4. Sludge, dust, dirt ,moisture can be removed by filtration.
  5. Oil when topped up shall be of the same make. It may lead to sludge formation and acidic contents.
  6. Insulation resistance of the transformer should be checked once in 6 months.
  7. Megger values along with oil values indicate the condition of transformer.
  8. Periodic Dissolved Gas Analysis can be carried out.

MAINTENANCE BUSHINGS

  1. Bushings should be cleaned and inspected for any cracks.
  2. Dust & dirt deposition, Salt or chemical deposition, cement or acid fumes depositions should be carefully noted and rectified.

MAINTENANCE

  1. Periodic checking of any loose connections of the terminations of HV & LV side.
  2. Breather examination. Dehydration of Silica gel if necessary.
  3. Explosion vent diaphragm examination.
  4. Conservator to be cleaned from inside after every three years.
  5. Regular inspection of OIL & WINDING TEMPERATURE METER readings.
  6. Cleanliness in the Substation yard with all nets, vines, shrubs removed.

 

Work on distribution transformers

When work is to be carried out on the connections to, or the windings of, a distribution transformer:

a.  the Authorised Person (HV) should record
the details of necessary safety precautions  and switching operations on a safety programme, and produce an isolation and earthing diagram;
b.  the switchgear or fuse gear controlling the high voltage windings should be switched off, and a safety lock and caution sign fitted;
c.  the low voltage windings of the transformer switch or isolator should be switched off, and a safety lock and caution sign fitted, or other physical means should be used to prevent the switch being energised during the course of work;
d.  where applicable, danger signs should be attached on or adjacent to the live electrical equipment at the limits of the zone in which work is to be carried out;
e.  the transformer should be proved dead at the points-of-isolation if practicable;
f.  an earth should then be applied to the high voltage winding via the switchgear and a safety lock fitted. If the proprietary earthing gear is available for the low voltage switchgear, it should be fitted and safety locks applied (it is advisable to retest for dead before fitting this earthing gear);
g.  before a permit-to-work is issued – the Authorised Person (HV) should, at the point- of-work in the presence of the Competent
Person (HV), identify and mark the transformer to be worked on. The permit-to-work and the key to the key safe should then be issued to the Competent Person (HV);

PROTECTION OF TRANSFORMERS

  1. The best way of protecting a transformer is to have good preventive maintenance schedule.
  2. Oil Temperature Indicators.
  3. Winding Temperature indicators.
  4. Buchholz Relay.
  5. Magnetic Oil level Gauge.
  6. Explosion Vent.
  7. HT fuse & D.O. fuse.
  8. LT circuit breaker.
  9. HT Circuit breaker with Over load, Earth Fault relay tripping.
  10. Oil Surge Relay for OLTC.
  11. PRV for OLTC.
  12. HORN GAPS & Lightening Arrestor.
  13. Breather.

FAILURES & CAUSES

  • Insufficient Oil level.
  • Seepage of water in oil.
  • Prolonged Over loading.
  • Single Phase loading.
  • Unbalanced loading.
  • Faulty Termination (Improper sized lugs etc)
  • Power Theft.
  • Prolonged Short Circuit.
  • Faulty operation of tap changer switch.
  • Lack of installation checks.
  • Faulty design
  • Poor Workmanship

-Improper formation of core.

– Improper core bolt insulation.

– Burr to the lamination blades

– Improper brazing of  joints.

– Burr /sharp edges to the winding conductor.

– Incomplete drying.

– Bad insulation covering.

– Insufficient cooling ducts in the winding.

  • Bad Quality of raw material.
  • Transit damaged transformers.
  • After failure , transformer is removed and replaced with new/repaired one without removing the cause of failure which results in immediate or short time failure.

HIGH VOLTAGE EQUIPMENT MAINTENANCE

  1. MAINTENANCE OF SWITCHGEAR ENCLOSURES
  2. Strictly adhere to required procedures for system switching operations. Switching, de-energizing and energizing shall be performed by authorized personnel only.
  3. Install temporary grounding leads for safety.
  4. Remove necessary access and coverplates.
  5. Fill out inspection test form. Record data in reference to equipment.
  1. Completely isolate switchgear enclosure to be tested and inspected from sources of power.
  1. Mechanical Inspection:
    I. Check mechanical operation of devices.
    II. Check physical appearance of doors, devices, equipment and lubricate in accordance with manufacturer’s instructions.
    III. Check condition of contacts.
    IV. Check disconnects, starters, and circuit breakers in accordance with inspection and test reports and procedures.
    V. Check condition of bussing for signs of overheating, moisture or other contamination, for proper torque, and for clearance to ground.
    VI. Inspect insulators and insulating surfaces for cleanliness, cracks, chips, tracking.
    VII. Report discovered unsafe conditions.
    VIII. Remove drawout breakers and check drawout equipment.
    IX. Check cable and wiring condition, appearance, and terminations. Perform electrical tests as required.
    X. Inspect for proper grounding of equipment.
    XI. Perform breaker and switch inspection and tests
  2. Cleaning:
    i. Check for accumulations of dirt especially on insulating surfaces and clean interiors of compartments thoroughly using a vacuum or blower.
    ii. Remove filings caused by burnishing of contacts.
    iii. Do not file contacts. Minor pitting or discoloration is acceptable.
    iv. Report evidence of severe arcing or burning of contacts.
    v. Degrease contacts with suitable cleaners
  3. Electrical Testing:
    i. Check electrical operation of pilot devices, switches, meters, relays, auxiliary contacts, annunciator devices, flags, interlocks, cell switches, cubicle lighting.  Visually inspect arrestors, C/T’s and P/T’s for signs of damage.  Record data on test report form.
    ii.  Megger test insulators to ground.
    iii.  Megger test bussing phase to ground, and phase to phase, using a 1000 volt megger.
    iv.  DC hipot phases to others and to ground using step voltage method as specified for cables with withstand levels held for not less than one minute.  Record decay curve, current versus time to completion of test, and indicate withstand level.
    .
  4. Electrical Testing:v. Maximum DC hipot test levels shall be as follows:
    a) 25kV class       50kV DC
    b)       15kV class       28.5kV DC
    c)       5kV class         9kV DC

    vi.  Test contact resistance across bolted sections of buss bars.  Record results and compare test values to previous acceptance and maintenance results and comment on trends observed.

    9. At completion of inspection and test, remove temporary grounds, restore equipment to serviceable condition and recommission equipment.

    10. Compare test results to previous maintenance test results

  5. MAINTENANCE OF HIGH VOLTAGE AIR/OIL CIRCUIT BREAKERS:1. Strictly adhere to required procedures for system switching operations. Switching, de-energizing and energizing shall be performed by authorized personnel only.

    2. Completely isolate circuit breakers to be worked on from power sources.
    3. Install temporary grounds.
    4. Remove circuit breaker from cubicle unless bolted type.
    5. Record manufacturer, serial number, type and function of breaker, reading of operations counter, date of inspection, and signature of person responsible for inspection on report sheet.

  6. Mechanical Inspection:
    Inspect for:
    I. accumulations of dirt, especially on insulating surfaces.
    II. condition of primary contact clusters.
    III. condition of control wiring plug-in contacts.
    IV. condition of moving and fixed main contacts, excessive heating or arcing.
    V. condition of arcing contacts.
    VI. cracks or indications of tracking on insulators.
    VII. tracking or mechanical damage to interphase barriers.
    VIII.flaking or chipping of arc chutes.
    IX. broken, damaged or missing springs on operating mechanism.
    X. damage to or excessive wear on operating linkage, ensure all clevis pins are securely retained in position.

Inspect for:
XI. correct alignment of operating mechanism and contacts.
XII. evidence of corrosion and rusting of metals, and deterioration of painted surfaces.

XIII. Oil breakers only:
a)  Refer to manufacturer’s maintenance manual for special tools that may be required to check oil breaker contacts.
b)  Check oil holding tanks in accordance with manufacturer’s instructions.
c)  Check for proper oil level and condition of level gauge.

  1. Cleaning:
    i. Remove accumulations of dirt from insides of cubicles with vacuum cleaner and/or blower.
    Ii.  Clean insulating surfaces using brush or wiping with lint free cloth.8. Check fixing bolts of hardware and breaker components for tightness.

    9.  ‘Dress’ pitting on contact surfaces, using a burnishing tool.  ‘Dress’ major arcing on contacts to smooth condition.  Remove filings before switchgear is re-energized.  Report unsafe conditions resulting from severe arcing or burning of contacts.

  2. On completion of foregoing tasks, lightly lubricate bearing points in operating linkage with manufacturer’s specified lubricant. Operate breaker several times to ensure smoothness of mechanical operation.11. Check potential and current transformer cable connections for tightness.

    12.  Replace inspection lamp where fitted.

    13.  On first inspection, record data to auxiliary equipment, i.e. primary fuses, potential transformer, potential fuses, and current transformers.  Record serial numbers, catalogue numbers, sizes, ratios.
    14.  On completion of inspection and test, remove temporary grounds.  Restore equipment to serviceable condition.

  3. Electrical Maintenance Tests:
    a) General:
    i.   Test contact resistance across closed line-load contacts, and line and load circuit breaker plug-in clusters.  Record results.  Clean contacts using appropriate tools to get lowest contact resistance reading possible.
    ii.   Test insulation resistance for all phases to others and to ground.
    iii.   Test electrical function in accordance with breaker manufacturer’s instructions and drawings.b)    Air Breakers:
    i.  Prior to hipot test being carried out, ensure surrounding primary connections to main equipment are properly grounded and isolated.
    ii.  DC hipot test at test levels indicated for switchgear enclosure.

    c)   Oil Breakers:
    i.   Do not perform DC hipot tests on oil circuit breakers.
    ii.   Dielectric (hipot) test on insulating oil per ASTM D877.  Compare dielectric strength test results to previous test data where applicable, and comment on changes.

FUSED OR UNFUSED LB AND NLB DISCONNECT SWITCHGEAR

.1       Strictly adhere to required procedures for system switching operations.  Switching, de-energizing and energizing shall be performed by authorized personnel only.

.2       Completely isolate switchgear to be worked on from power sources.

.3       Remove access covers and plates.

.4       Test and discharge equipment to be worked on.

.5       Install temporary safety grounds.

.6       Report manufacturer, serial number, type, function of switchgear assembly, date of inspection, and signature of person responsible for inspection.

  1. Mechanical Inspection: inspect for:
    I.  accumulations of dirt, especially on insulating surfaces.
    II.  condition of moving and fixed contact, excessive heating or arcing.
    III.  cracks, or tracking on insulators.
    IV.  tracking or mechanical damage to interphase barriers.
    V.  chipping or flaking of arc chutes or arc shields.
    VI.  fixing bolts being fully tightened where bolted-on shields are fitted.
    VII.  overheating or arcing on fuses and fuse holders.
    VIII.   correct fuse clip tension.
    IX.   broken, missing or damaged springs on operating mechanism.
    X.   damage to or excessive wear on operating linkage.  Check that all clevis pins are securely retained in position.
    XI.   correct alignment of contact blades and operating linkage.
    XII.   corrosion & rusting of metals, deterioration of painted surfaces.
    XIII.   proper operation of key interlock or other mechanical interlock (if applicable).
    XIV.   evidence of corona deterioration.
  2. Cleaning:I. Remove accumulations of dirt from insides of switchgear cubicles using vacuum cleaner and/or blower.
    II.   Clean insulating surfaces using brush or wiping with lint free cloth.
    III.   Do not file contacts.  Minor pitting or discoloration is acceptable.
    IV.   Report evidence of severe arcing or burning of contacts.
    V.   Degrease contacts with suitable cleaners.

    9. Check that connections, including current limiting fuses, are secure.  Torque to manufacturer’s requirement.

  3. Electrical Maintenance Tests:
    I.  Test insulation resistance for all phases to others and to ground.
    II.  Test contact resistance across switch blade contact surfaces.
    III.  Test electrical charging mechanism of switch if applicable.
    IV.  Test electrical interlocks for proper function.
    V.   DC hipot test phases to the others and to ground using step method to levels specified for switchgear.
    VI.   Operate blown fuse trip devices if applicable.11.  After testing is completed, remove temporary grounds and restore equipment to serviceable condition.
  4. MAINTENANCE OF PROTECTION RELAYS1. Strictly adhere to required procedures for system switching operations. Switching, de-energizing and energizing shall be performed by authorized personnel only.

    2.   Completely isolate protective relays to be tested and inspected from sources of power.

    3.   Set and test protective relays to “as found” settings or to new settings provided by Minister prior to maintenance commissioning.

    4.   Use manufacturer’s instructions for information concerning connections, adjustments, repairs, timing, and data for specific relay.

  5. Mechanical Inspection of Induction Disc Relays:
    I. Carefully remove cover from relay case.  Inspect cover gasket.  Check glass for tightness and cracks.
    II.   Short-circuit current transformer secondary by careful removal of relay test plug or operation of appropriate current blocks.
    III.   Ensure disc has proper clearance and freedom of movement between magnet poles.
    IV.   Check connections and taps for tightness.
    V.   Manually operate disc to check for freedom of movement.  Allow spring to return disc to check proper operation.
    VI.   Check mechanical operation of targets.
    VII.   Check relay coils for signs of overheating and brittle insulation
  6. Cleaning:
    I.  Clean glass inside and out.
    II.  Clean relay compartment as required.  Clean relay plug in contacts, if applicable, using proper tools.
    III.   Remove dust and foreign materials from interior of relay using small brush or low pressure (7 lbs.) blower of nitrogen.
    IV.   Remove rust or metal particles from disc or magnet poles with magnet cleaner or brush.
    V.   Inspect for signs of carbon, moisture and corrosion.
    VI.   Clean pitted or burned relay contacts with burnishing tool or non-residue contact cleaner.
  7. Electrical Testing: Tests for typical overcurrent relays include:
    I.  Zero check.
    II.   Induction disc pickup.
    III.  Time-current characteristics.
    IV.   Target and seal-in operation.
    V.   Instantaneous pickup.
    VI.   Check C/T & P/T ratios and compare to coordination data.
    VII.   Proof test each relay in its control circuit by simulated trip tests to ensure total and proper operation of breaker and relay trip circuit by injection of the relay circuit to test the trip operation.
  8. Solid State Relays:
    I. Inspect and test in accordance with manufacturer’s most recent installation and maintenance brochure.
    II.   Perform tests using manufacturer’s relay test unit as applicable, with corresponding test instructions.
    III.   If the manufacturer’s tester is not available, use a relay tester unit approved by relay manufacturer, with proper test data and test accessories.
    IV.   Proof test each relay in its control circuit by simulated trip tests to ensure total and proper operation of breaker and relay trip circuit by injection of relay circuit to test trip operation.
    V.   Check C/T and P/T ratios and compare to coordination date.9.   At completion of inspection and test, restore equipment to serviceable condition and recommission equipment.  Compare test results to previous maintenance test results.
  9. MAINTENANCE OF OVERHEAD RADIAL POWER LINES:1.

    Strictly adhere to required procedures for system switching operations. Switching, de-energizing and energizing shall be performed by authorized personnel only.
    2.  Completely isolate overhead radial power lines to be tested and inspected from sources of power.
    3.  Install temporary grounding leads for safety.
    4.  Inspect insulators and insulating surfaces for cleanliness, cracks, chips, tracking, and clean insulators thoroughly.

  10. Check cable connections to insulators and check cable sag between poles. Report discovered unsafe conditions.
    6.   Visually check wooden poles and sound test with 18 oz. wooden mallet.
    7.   Visually inspect metal line structures for rust, deterioration, metal fatigue, and report discovered unsafe conditions.
    8.   Inspect crossarms, bolts, rack assemblies, guys, guy wires, and dead ends.  Report discovered unsafe conditions.
    9.   Visually inspect grounding connections.
    10.   On completion of inspection, remove temporary grounding, restore equipment to serviceable condition
  11. SURGE ARRESTORS:
    1. Strictly adhere to required procedures for system switching operations.  Switching, de-energizing and energizing shall be performed by authorized personnel only.
    2.   Completely isolate surge arrestors to be tested and inspected from sources of power.
    3.   Install temporary grounding leads for safety.
    4.   Inspect surge arrestors for cleanliness, cracks, chips, tracking and clean thoroughly.
    5.   Perform insulation power factor test.  Record results.
    6.   Perform grounding continuity test to ground grid system, record results.
    7.  On completion of inspection and testing, remove temporary grounds, restore equipment to serviceable condition.

DISCONNECTION PROCEDURE:

Safety of Disconnection Switch:
1.  When a disconnect switch is installed in this manner, the frame of the disconnect switch, the upper and lower steel operating rod and the switch handle are all bonded together and connected to the common neutral and the pole’s ground rod, effectively eliminating any insulating value of the insulated insert. The electrical worker operating the switch has no protection and could have as much as full system voltage from the worker’s hands on the switch handle to the worker’s feet.
2.  The use of rated rubber gloves can eliminate touch potential if the switch were to fail and go to ground. But there is also the hazard of step potential for the worker operating the switch, and rated rubber gloves does nothing to eliminate step potential. Also, the maximum ASTM rating for rubber gloves is limited to 36 kV, eliminating worker protection from higher voltages.
3.  Properly installed ground mats provide the best protection for workers operating disconnect switches while standing on the ground.

If the disconnect switch were to fail and go to ground, the switch handle could be energized at potentially full system voltage, say 7,200 volts, energizing the switch handle at 7,200 volts, less the voltage drop in the grounding conductor from the switch handle to the ground mat (typically 20 to 25 volts).

–  But if the worker were wearing rated rubber gloves and standing on a ground mat attached to the switch handle, would they be safe? Yes!

–  If they were not wearing rated rubber gloves but still standing on a ground mat attached to the switch handle, would they be safe? Yes!

–  When the worker wears rated rubber gloves while standing on a ground mat attached to the switch handle, the gloves are insulating the worker from the 20 to 25 volts developed across the ground mat and switch handle; well below any hazardous voltage. They are safe with or without rated rubber gloves if they are standing on a ground mat properly connected to the switch handle.

PPE to WORK in HV

HV Disconnection Procedure:
Almost every major line or equipment in a substation has associated with it a means of completely isolating it from other energized elements as a prudent means of insuring safety by preventing accidental energization. These simple switches, called disconnects, or disconnecting switches. They are usually installed on both sides of the equipment or line upon which work is to be done.

How to operate these switches:
1. They should not be operated while the circuit in which they are connected is energized, but only after the circuit is deenergized.
2. They may be opened by means of an insulated stick that helps the operator keep a distance from the switch.
3. Locking devices are sometimes provided to keep the disconnects from being opened accidentally or from being blown open during periods of heavy fault currents passing through them.

ISOLATION OF ANY HIGH VOLTAGE EQUIPMENT:

What is isolation:
Isolation is a means of physically and electrically separating two parts of a measurement device, and can be categorized into electrical and safety isolation. Electrical isolation pertains to eliminating ground paths between two electrical systems. By providing electrical isolation, you can break ground loops, increase the common-mode range of the data acquisition system, and level shift the signal ground reference to a single system ground. Safety isolation references standards have specific requirements for isolating humans from contact with hazardous voltages. It also characterizes the ability of an electrical system to prevent high voltages and transient voltages from transmitting across its boundary to other electrical systems with which you can come in contact.

  1. Isolation of individual circuits protected by circuit breakersWhere circuit breakers are used the relevant device should be locked-off using an appropriate locking-off clip with a padlock which can only be opened by a unique key or combination. The key or combination should be retained by the person carrying out the work.

    Note
    Some DBs are manufactured with ‘Slider Switches’ to disconnect the circuit from the live side of the circuit breaker. These devices should not be relied upon as the only means of isolation for circuits as the wrong switch could easily be operated on completion of the work.

  2. Isolation of individual circuits protected by fuses
    Where fuses are used, the simple removal of the fuse is an acceptable means of disconnection. Where removal of the fuse exposes live terminals that can be touched, the incoming supply to the fuse will need to be isolated. To prevent the fuse being replaced by others, the fuse should be retained by the person carrying out the work, and a lockable fuse insert with a padlock should be fitted as above. A caution notice should also be used to deter inadvertent replacement of a spare fuse. In addition, it is recommended that the enclosure is locked to prevent access as stated above under ‘Isolation using a main switch or distribution board (DB) switch-disconnector’.Note
    In TT systems, the incoming neutral conductor cannot reliably be regarded as being at earth potential. This means that for TT supplies, a multi-pole switching device which disconnects the phase and neutral conductors must be used as the means of isolation. For similar reasons, in IT systems all poles of the supply must be disconnected. Single pole isolation in these circumstances is not acceptable.
    High voltage insulation testing (flash testing) can be particularly hazardous when several parts of the equipment are energized for a period of time.

Isolation Procedure:
1. Isolate from all sources of supply.
2. Prevent unauthorised connection by fixing safety locks and caution signs at points-of- isolation.
2. Fix danger signs on live equipment adjacent to the point-of-work.
PROVING THE SYSTEM IS DEAD:

How to prove:
Before starting work it should be proved that the parts to be worked on and those nearby are dead. It should never be assumed that equipment is dead because a particular isolation device has been placed in the off position.
1. The procedure for proving dead should be by use of a proprietary test lamp or two pole voltage detectors.
2. Non-contact voltage indicators (voltage sticks) and multi-meters should not be used.
3. The test instrument should be proved to be working on a known live source or proprietary proving unit before and after use.
4. All phases of the supply and the neutral should be tested and proved dead.

Proving dead unused or unidentified cables
• Where there is uncertainty regarding isolation when removing unidentified cables or proving dead an ‘unused’ cable, particularly where insufficient conductor is exposed to enable the use of test probes, those conductors should be assumed to be live until positively proven to be dead and any work carried out on them should employ live working practices until the conductors are proved dead.
• Clamp meters can be used as a means of identifying cables by testing for current flow in the conductors.
•  Non-contact voltage indicators (voltage sticks) can also be useful in these situations to test for voltage where cables without a metallic sheath are to be identified. However, once insulation is pared using live working practices to reveal the underlying conductors, contact voltage detectors should be used as the means of proving dead.

Prove Dead:
(i) Prove dead with a high voltage potential indicator at all accessible points-of-isolation.
(ii) Where appropriate, prove dead on the low voltage side of a transformer, that is LV feed pillars, LV distribution boards etc.

EARTHING AND DISCHARGING OF HV:

Earthing down is a very important concept to understand when working with high voltage systems.
It is important to ensure that any stored electrical energy in equipment insulation after isolation is safely discharged to earth.
The application of earthing on high voltage conductors is controlled in accordance with the provisions of the Power System Safety Rules.
The following general requirements and principles are applicable for portable earthing.

Safety:
1.  Always carry earthing equipment below shoulder level;
2. Ensure that clamps and leads are kept a safe distance from any high voltage conductor;
3. Apply clamps to stirrup (if provided) or a horizontal conductor where possible;
4. Avoid clamp application to bushing caps and to braids; and
5. Position clamp so that tension on the earth lead is minimised.
6. Assemble and inspect earthing equipment on the ground;
7. Extend or otherwise prepare any earthing equipment such as shot gun sticks on the ground.
8. Proving High Voltage Conductors De-Energised
9. Do not allow any part of the earthing system to encroach on safe approach distances. Where practicable, keep the earthing leads away from the body;
10. Earthing equipment is to be removed carefully from high voltage conductors to prevent the equipment encroaching on or coming into contact with adjacent live high voltage conductors.
11. Check that the rating of the earthing equipment is appropriate for the fault level at the location at which it is to be applied.
12. Ensure that the earthing equipment is in a serviceable condition. Any portable earthing equipment found to be defective shall be removed from service for repair or disposal.

There are two types of earthing down a high voltage switchboard:

1. CIRCUIT EARTHING
– an incoming or outgoing feeder cable is connected by a heavy earth connection from earth to all three
conductors after the circuit breaker has been racked out. This is done at the circuit breaker using a special key. This key is then locked in the key safe. The circuit breaker cannot be racked in until the circuit earth has been removed.

2. BUSBAR EARTHING
– when it is necessary to work on a section of the
busbars, they must be completely isolated from all possible electrical sources. This will include generator incoming cables, section or bus-tie breakers, and transformers on that busbar section. The busbars are connected together and earthed down using portable leads, which give visible confirmation of the earthing arrangement.

Earthing Procedure:
(i) Earth conductors at all points-of-isolation and fix safety locks to earths.
(ii) Identify with certainty or spike underground cables at the point/s of work if the conductors are to be cut or exposed.
(iii) Earth overhead lines near the working places.

ISSUING OF A PERMIT-TO-WORK or
SANCTION- FOR-TEST:

1. Before a permit-to-work or a sanction-for-test is issued, the Authorised Person or Electrical Engineer should identify the equipment on which the work or test is to be undertaken.
2. If the work involves, or may involve, obtaining access to items of equipment over which confusion could occur, the Authorised Person (HV)/ Electrical Engineer should identify such items to the Competent Person (HV) and apply temporary marking to them.
3. Before issuing a permit-to-work or sanction-for- test, the Authorised Person (HV)/ Electrical Engineer should show the Competent Person (HV) the isolation and earthing diagram and indicate the safety arrangements at the points-of-isolation and at the point-of-work or test.

  1. The Authorised Person (HV)/ Electrical Engineer should ensure that the Competent Person (HV) understands all the relevant safety procedures and precautions.
    5. If the Competent Person (HV) thereafter accepts the permit or sanction, that person becomes responsible for the defined work or test until the permit or sanction is cancelled.
    6. Mark the point-of-work.
    7. Issue the permit-to-work, isolation and earthing diagram, and the key to the safety key box to the Competent Person (HV).
    8. Authorised Persons (HV)/ Electrical Engineer undertaking tasks requiring permits-to-work or sanctions-for-test should issue the documents to themselves.
    9. Adjust mimic diagram and complete the site logbook.
    10. All such documents must be countersigned by a site- certified Authorised Person (HV)/ Electrical Engineer before the work or test starts.

Undertake the work:
The Competent Person (HV) is to undertake or directly supervise the work and on completion, or when the work is stopped and made safe, is to return the original of the permit-to-work, the isolation and earthing diagram and the Competent Person’s (HV) key to the safety key box to the Duty Authorised Person (HV)/ Electrical Engineer, and complete part 3 of the permit retained in the pad.

Check the equipment:
If the work has been completed, check to ensure it is safe to energize. If the work has been stopped, check the equipment has been made safe.

Cancel the permit-to-work:
(i)  Cancel the permit-to-work by signing the “completion of work” part  and by cancel the permit in the presence of the Competent Person (HV).
(ii)  File the isolation and earthing diagram in the operational procedure manual and permit-to-work in respective file.
(iii)  Return key to key safe.

Issue the sanction-for-test :
(i)   The Competent Person (HV) is to be shown the safety arrangements at all the point/s of isolation and at the locations of the test, and is to initial the isolation and earthing diagram.
(ii)  Issue the sanction-for-test, isolation and earthing diagram, and the key to the safety key box to the Competent Person (HV).
(iii)  Retain working lock keys, and remove and replace earths as requested.

Cancel the sanction-for-test:
(i) Cancel the sanction-for-test by signing part 4 and by destroying the sanction in the presence of the Competent Person (HV).
(ii) File the isolation and earthing diagram in the operational procedure manual.
(iii) Return key to key safe.

RE-ENERGIZING EQUIPMENT:

i. Conduct tests and visual inspections to ensure all tools, electrical jumpers, shorts, grounds, and other such devices have been removed.
ii. Warn others to stay clear of circuits and equipment.
iii. Each lock and tag must be removed by the person who applied it.
iv. Visually check that all employees are clear of the circuits and equipment.

PROTECTIONS OPERATING PRINCIPLES
SF6 Circuit Breaker
:
A circuit breaker in which the current carrying contacts operate in sulphur hexafluoride or SF6 gas is known as an SF6 circuit breaker.
SF6 has excellent insulating property. SF6 has high electro-negativity. That means it has high affinity of absorbing free electron. Whenever a free electron collides with the SF6 gas molecule, it is absorbed by that gas molecule and forms a negative ion.
The attachment of electron with SF6gas molecules may occur in two different ways,

These negative ions obviously much heavier than a free electron and therefore over all mobility of the charged particle in the SF6 gas is much less as compared other common gases. We know that mobility of charged particle is majorly responsible for conducting current through a gas.

Working of SF6 Circuit Breaker:
The working of SF6 CB of first generation was quite simple it is some extent similar to air blast circuit breaker. Here SF6 gas was compressed and stored in a high pressure reservoir. During operation of SF6 circuit breaker this highly compressed gas is released through the arc in breaker and collected to relatively low pressure reservoir and then it pumped back to the high pressure reservoir for re utilize.
The working of SF6 circuit breaker is little bit different in modern time. Innovation of puffer type design makes operation of SF6 CB much easier. In buffer type design, the arc energy is utilized to develop pressure in the arcing chamber for arc quenching.

During opening of the breaker the cylinder moves downwards against position of the fixed piston hence the volume inside the cylinder is reduced which produces compressed SF6 gas inside the cylinder. The cylinder has numbers of side vents which were blocked by upper fixed contact body during closed position. As the cylinder move further downwards, these vent openings cross the upper fixed contact, and become unblocked and then compressed SF6 gas inside the cylinder will come out through this vents in high speed towards the arc and passes through the axial hole of the both fixed contacts. The arc is quenched during this flow of SF6 gas.

During closing of the circuit breaker, the sliding cylinder moves upwards and as the position of piston remains at fixed height, the volume of the cylinder increases which introduces low pressure inside the cylinder compared to the surrounding. Due to this pressure difference SF6 gas from surrounding will try to enter in the cylinder. The higher pressure gas will come through the axial hole of both fixed contact and enters into cylinder via vent and during this flow; the gas will quench the arc.

PROTECTIONS OPERATING PRINCIPLES

Principles of Distance Relays
Since the impedance of a transmission line is proportional to its length, for distance measurement it is appropriate to use a relay capable of measuring the impedance of a line up to a predetermined point (the reach point).
Such a relay is described as a distance relay and is designed to operate only for faults occurring between the relay location and the selected reach point, thus giving discrimination for faults that may occur in different line sections.
The basic principle of distance protection involves the division of the voltage at the relaying point by the measured current. The apparent impedance so calculated is compared with the reach point impedance. If the measured impedance is less than the reach point impedance, it is assumed that a fault exists on the line between the relay and the reach point.
The reach point of a relay is the point along the line impedance locus that is intersected by the boundary characteristic of the relay.
Since this is dependent on the ratio of voltage and current and the phase angle between them, it may be plotted on an R/X diagram. The loci of power system impedances as seen by the relay during faults, power swings and load variations may be plotted on the same diagram and in this manner the performance of the relay in the presence of system faults and disturbances may be studied.

Solid State Switching Principle
– High voltage testing does not usually require high power.
Thus special methods may be used which are not applicable.
– Then generating high voltage in high power applications.
– In the field of electrical eng. & applied physics, high voltages are required for several applications  as:
1. a power supply (eg. hv dc) for the equipments such as electron microscope and x-ray machine.
2. required for testing power apparatus – insulation testing.

-High impulse voltages are required for testing purposes to simulate over voltages due to lightning and switching.

Solid State Switching Principle

Solid State Switching Principle

  • Both full-wave as well as half-wave circuits can produce a maximum direct voltage corresponding to the peak value of the alternating voltage.
  • When higher voltages are required voltage multiplier circuits are used. The common circuits are the voltage double circuit
  • Used for higher voltages.
  • Generate very high dc voltage from single supply transformer by extending the simple voltage doubler circuit.

Electric Propulsion and High Voltage Practice

Marine Electric Propulsion

Integrated electric propulsion (IEP) or full electric propulsion (FEP) or integrated full electric propulsion (IFEP) is an arrangement of marine propulsion systems such that gas turbines or diesel generators or both generate three phase electricity which is then used to power electric motors turning either propellers.

It is a modification of the combined diesel-electric and gas propulsion system for ships which eliminates the need for clutches and reduces or eliminates the need for gearboxes by using electrical transmission rather than mechanical transmission of energy.

Electric propulsion for many new ships is now re-established as the popular choice where the motor thrust is governed by electronic switching under computer control.

The high power required for electric propulsion usually demands a high voltage (HV) power plant with its associated safety and testing procedures.

Passenger ships have always been the largest commercial vessels with electric propulsion and, by their nature, the most glamorous. This should not, however, obscure the fact that a very wide variety of vessels have been, and are, built with electric propulsion.

Early large passenger vessels employed the turboelectric system which involves the use of variable speed, and therefore variable frequency, turbo-generator sets for the supply of electric power to the propulsion motors directly coupled to the propeller shafts. Hence, the generator/motor system was acting as a speed reducing transmission system. Electric power for auxiliary ship services required the use of separate constant frequency generator sets.

A system that has generating sets which can be used to provide power to both the propulsion system and ship services has obvious advantages, but this would have to be a fixed voltage and frequency system to satisfy the requirements of the ship service loads. The provision of high power variable speed drives from a fixed voltage and frequency supply has always presented problems. Also, when the required propulsion power was beyond the capacity of a single d.c. motor there was the complication of multiple motors per shaft.            

Developments in high power static converter equipment have presented a very convenient means of providing variable speed a.c. and d.c. drives at the largest ratings likely to be required in a / marine propulsion system.

The electric propulsion of ships requires electric motors to drive the propellers and generator sets to supply the electric power. It may seem rather illogical to use electric generators, switchgear and motors between the prime-movers (e.g. diesel engines) and propeller when a gearbox or length of shaft could be all that is required.

There are obviously sound reasons why, for some installations, it is possible to justify the complication of electric propulsion:

  1. Flexibility of layout
  2. Load diversity between ship service load and propulsion
  3. Economical part-load running
  4. Ease of control
  5. Low noise and vibration characteristics

FLEXIBILITY OF LAYOUT

The advantage of an electric transmission is that the prime-movers, and their generators, are not constrained to have any particular relationship with the load as a cable run is a very versatile transmission medium. In a ship propulsion system it is possible to mount the diesel engines, gas turbines etc., in locations best suited for them and their associated services, so they can be remote from the propeller shaft. Diesel generator sets in containers located on the vessel main deck have been used to provide propulsion power and some other vessels have had a 10 MW generator for ship propulsion duty mounted in a block at the stern of the vessel above the ro-ro deck.

Another example of the flexibility provided by an electric propulsion system is in a semi-submersible, with the generators on the main deck and the propulsion motors in the pontoons at the bottom of the support legs.
LOAD DIVERSITY

Certain types of vessels have a requirement for substantial amounts of electric power for ship services when the demands of the propulsion system are low. Tankers are one instance of this situation and any vessel with a substantial cargo discharging load also qualifies. Passenger vessels have a substantial electrical load which, although relatively constant, does involve a significant size of generator plant. There are advantages in having a single central power generation facility which can service the propulsion and all other ship loads as required.

ECONOMICAL PART-LOAD RUNNING

Again this is a concept that is best achieved when there is a central power generation system feeding propulsion and ship services, with passenger vessels being a good example.

It is likely that a typical installation would have between 4-8 diesel generator sets and with parallel operation of all the sets it becomes very easy to match the available generating capacity to the load demand. In a four engine installation for example, increasing the number of sets in operation from two that are fully loaded to three partially loaded will result in the three sets operating at a 67% load factor which is not ideal but also not a serious operating condition, It is not necessary to operate generating sets at part-load to provide the spare capacity to be able to cater for the sudden loss of a set, because propulsion load reduction may be available instantaneously, and in most vessels a short time reduction in propulsion power does not constitute a hazard.

The propulsion regulator will continuously monitor the present generator capability and any generator overload will immediately result in controlled power limitation to the propulsion motors. During manoeuvring, propulsion power requirements are below system capacity and failure of one generator is not likely to present a hazardous situation.

EASE OF CONTROL

The widespread use of controllable pitch propellers (cpp) has meant that the control facilities that were so readily available with electric drives are no longer able to command the same premium. Electric drives are capable of the most exacting demands with regard to dynamic performance which, in general, exceed by a very wide margin anything that is required of a ship propulsion system.

 LOW NOISE

An electric motor is able to provide a drive with very low vibration characteristics and this is of importance in warships, oceanographic survey vessels and cruise ships where,/-for different reasons, a low noise signature is required. With warships and survey vessels it is noise into the water which is the critical factor whilst with cruise ships it is structure borne noise and vibration to the passenger spaces that has to be minimised.

For very high power, the most favoured option is to use a pair of high efficiency, high voltage a.c. synchronous motors with fixed pitch propellers (FPP) driven at variable speed by frequency control from electronic converters. A few installations have the combination of controllable pitch propellers (CPP) and a variable speed motor. Low/medium power propulsion (1-5 MW) may be delivered by a.c. induction motors with variable frequency converters or by d.c. motors with variable voltage converters.

The prime-movers are conventionally constant speed diesel engines driving a.c. generators to give a fixed output frequency. Gas turbine driven prime- movers for the generators are likely to challenge the diesel option in the future.

Conventionally, the propeller drive shaft is directly driven from the propulsion electric motor (PEM) from inside the ship. From experience obtained from smaller external drives, notably from ice-breakers, some very large propulsion motors are being fitted within rotating pods mounted outside of the ship’s hull. These are generally referred to as azipods , as the whole pod unit can be rotated through 360° to apply the thrust in any horizontal direction, i.e. in azimuth. This means that a conventional steering plate and stern side-thrusters are not required.

Ship manoeuvrability is significantly enhanced by using azipods and the external propulsion unit releases some internal space for more cargo/passengers while further reducing hull vibration.

Gradual progress in the science and application of superconductivity suggests that future generators and motors could be super-cooled to extremely low temperatures to cause electrical resistance to become zero.

Marine Electric Propulsion

– Podded drives offer greater propulsion efficiency and increased space within the hull by moving the propulsion motor outside the ships hull and placing it in a pod suspended underneath the hull.
– Podded drives are also capable of azimuth improving ship maneuverability. Indeed, podded drives have been widely adopted by the cruise ship community for these reasons.
– The motors being manufactured now are as large as 19.5 MW, and could provide the total propulsion power.

– In an AC drive, a frequency converter is used to control the speed and torque of electric motor. The speed of the AC electric motor can be controlled by varying the voltage and frequency of its supply. A frequency converter works by changing the constant frequency main electrical supply into a variable frequency output.

– The ideal simplicity of the induction motor, its perfect reversibility and other unique qualities render it eminently suitable for ship Propulsion.

Electric propulsion
– Diesel-Generator sets to produce electricity to common grid for propulsion and ship use.
– Variable speed drives to rotate fixed pitch propellers.
– Commonly used in Cruise vessels, LNG tankers, Off-shore vessels and Ice breaking vessels due to reduced fuel oil consumption, lower emissions and increased pay-load

  • Large Diesel Engine for Main Engine
  • Configuration of Electric Propulsion
  • System for Ships
  • Configuration of Electric Propulsion
  • System for Ships
  • Configuration of Electric Propulsion
  • System for Ships
  • Configuration of Electric Propulsion
  • Configuration of Electric Propulsion
  • System for Ships
  • Configuration of Electric Propulsion
  • System for Ships
  • Configuration of Electric Propulsion
  • System for Ships
  • Comparison with Conventional and
  • Electric Propulsion system

SHORE SUPPLY FACILITIES
Shore power supply facilities have adopted high voltage rather than low voltage by necessity in order to keep the physical size of related electrical equipment such as shore connection cables manageable.
Inevitably high voltage would otherwise introduce new risks to ship’s crew and the shipboard installations if necessary safety features were not built into the HVSC system or safe operating procedures were not put in place.

Those onboard systems that are designed to accept high voltage shore power, typically involving the following things:
– incoming power receptacles,
– shore connection switchgear,
– step-down transformer or isolation transformer,
– fixed power cables,
– incoming switchgear at the main switchboard and
– associated instrumentation. HVSC is often referred to as cold ironing.

The system nominal voltage is considered to be in the range from 1 kv ac to 15 kv ac.

Infrastructure Considerations

Electrical System Grounding Philosophy:

The manner in which electrical system is grounded (e.g., ungrounded system, solid neutral grounding system, low impedance neutral grounding system, or high impedance neutral grounding system), including ground potential transformer method. Circuit.

protection strategy is built around the selected method of system grounding in terms of over voltage prevention, over current prevention or continued operability under single phase grounded condition.

SYSTEM GROUNDING COMPATIBILITY

Arrangements are to be provided so that when the shore connection is established, the resulting system grounding onboard is to be compatible with the vessel’s original electrical system grounding philosophy (for instance, the shipboard ungrounded power distribution system is to remain ungrounded, or the shipboard high impedance grounding system is to remain high impedance grounded within the design grounding impedance values). Ground fault detection and protection is to remain available after the shore connection has been established.

Cable Management System:
The cable management  system is the ship’s interface point with the shore power system. The cable management  system is typically composed of flexible hv cables with the plug that extends to the shore power receptacle, cable reel, automatic tension control system with associated control gears, and instrumentation. shore power is fed to the shore connection switchboard via the cable management  system.

SHORE CONNECTION SWITCHBOARD

where no cable management  system is provided onboard, the shore connection switchboard is normally the ship’s interface point with the shore power system. hv shore power is connected to this shore connection switchboard by means of an hv plug and socket arrangement.  the shore connection switchboard is provided with a shore power connecting circuit breaker with circuit protection devices.

ONBOARD RECEIVING SWITCHBOARD

The receiving switchboard is normally a part of the ship’s main switchboard to which the shore power is fed from the shore connection switchboard.

EQUIPOTENTIAL BONDING

Equipotential bonding between the ship and the shore is to be provided. An interlock is provided such that the HV shore connection cannot be established until the equipotential bonding has been established. The bonding cable may be integrated into the HV shore power cable. If the equipotential bonding cable is intended to carry the shipboard ground fault current, the cable size is to be sufficient to carry the design maximum ground fault current.
LOAD TRANSFER

Temporary Parallel Running:
Where the shipboard generator is intended to run in parallel with the shore power for a short period of time for the purpose of connecting to the shore power or back to ship power without going through a blackout period, the following requirements are to be complied with:
i) Means are to be provided to verify that the incoming voltage is within the range for which the shipboard generator can be adjusted with its automatic voltage regulator (AVR)
ii) Means are to be provided for automatic synchronization
iii) Load transfer is to be automatic
iv) The duration of the temporary parallel running is to be as short a period as practicable allowing for the safe transfer of the load. In determining the rate of the gradual load transfer, due regard is to be paid to the governor characteristics of shipboard generator in order not to cause excessive voltage drop and frequency dip.

Load Transfer via Blackout

Where load transfer is executed via blackout (i.e., without temporary generator parallel running), safety interlock arrangements  are to be provided so that the circuit breaker for the shore power at the shore connection switchboard cannot be closed while the HV switchboard is live with running shipboard generator(s).

Safety Interlocks

An interlock, which prevents plugging and unplugging of the HV plug and socket outlet arrangements while they are energized, is to be provided.

Marine Shore Connection Concept

Shore Connection System Solutions
(Example)
On board Installation

Handling of HV Plug

While the HV shore connection circuit breakers are in the open position, the conductors of the HV supply cables are to be automatically kept earthed by means of an earthing switch. A set of pilot contactors embedded  in the HV plug and socket-outlet may be used for this purpose. The earthing switch control is to be designed based on a fail-to-safe concept such that the failure of the control system will not result in the closure of the earthing switch onto the live HV lines.

HV Shore Connection Circuit Breakers

Arrangements are to be provided to prevent the closing of the shore connection circuit breaker when any of the following conditions exist:

i) Equipotential bonding is not established
ii) The pilot contact circuit is not established
iii) Emergency shutdown facilities are activated
iv) An error within the HV connection system that could pose an unacceptable risk to the safe supply of shoreside power to the vessel. These errors may occur within the alarm system, whether on board the ship or at the shoreside control position, or within any relevant
safety systems including those which monitor system performance.
v) The HV supply is not present

HVSC Circuit Breaker Control:

HV shore connection circuit breakers are to be remotely operated  away from the HVSC equipment.
HV shore connection circuit breakers are to be made only when it has been established that personnel are evacuated from the HV shore connection equipment compartments. The operation manual is to describe these established procedures.

HVSC Emergency Shutdown:

In the event of an emergency, the HV system shall be provided with shutdown facilities that immediately open the shore connection circuit breaker. These emergency shutdown systems are to be automatically activated.

Any of the following conditions are to cause emergency shutdown of the shore power supply:

i) Loss of equipotential bonding
ii) High tension level of HV flexible shore connection cable, or low remaining cable length of cable management  system
iii) Shore connection safety circuits fail
iv) The emergency stop button is used
v) Any attempts to disengage the HV plug while live (this may be achieved by the pilot

contactors embedded  in the plug and socket such that the pilot contactors disengage before the phase contactors can disengage)

Tests of HV Switchboards

Type Test

HV switchboards are to be subjected to an AC withstand voltage test in accordance with Table-2
or other relevant national or international standards. A test is to be carried out at the manufacturer’s test facility in the presence of the Surveyor.

Onboard Test

After installation onboard, the HV switchboard is to be subjected to an insulation resistance test in accordance with Table-2 in the presence of the Surveyor.
EQUIPMENT DESIGN:

Air Clearance
Phase-to-phase air clearances and phase-to-earth air clearances between non-insulated parts are to be not less than the minimum, as specified in Table

Creepage Distance

Creepage distances between live parts and between live parts and earthed metal parts are to be adequate for the nominal voltage of the system, due regard being paid to the comparative tracking index of insulating materials under moist conditions according to the IEC Publication 60112 and to the transient overvoltage developed by switching and fault conditions.

Shore Connection Switchboard:

Construction
The HV shore connection switchboard is to be designed, manufactured and tested in accordance with a recognized standard code of practice as given by IEC.
Circuit Breaker
i) Shore connection HV circuit breaker is to be equipped with low voltage protection (LVP)
ii) The rated short-circuit making capacity of the circuit breaker is not to be less than the prospective peak value of the short-circuit current
iii) The rated short-circuit breaking capacity of the circuit breaker is not to be less than the maximum prospective symmetrical short-circuit current
iv) HV shore connection circuit breaker is to be remotely operated

  • HV Circuit Breakers may beAir-Break (scarcely used)
    2. Oil-Break (not used in ships)
    3. Gas-Break (SF – 6 – Sulphur Hexafluoride)
    4. Vacuum-Break (Most Popular)

Reference Articles, Books and websites:
1. Electric Propulsion Systems for Ships by Dr. Hiroyasu Kifune
2.  Standard Safety of High Voltage by Chris Spencer
3. www.marineinsight.com
4. www.abb.com
5. Practical Marine Electrical Knowledge by D.T. Hall
6. Low and high voltage supply by Henning E. Larsen
7. www.imtech.com
8. www.skysail.info

“Bunkering Procedure”

The actual Bunkering operation is carried out with bunker checklists. In this article, emphasis is made on the checklists, safety precautions, SOPEP locker & SOPEP equipments, temperature & density correction to calculate the quantity of oil bunkered. Formula for calculation has been included.

Bunkering Oil

Earlier we learnt about the bunkering and what is means. Now we will study the process of actual bunkering operations and the practical details of the process of bunkering oil. All types of ships needs fuel oil, lub oil etc and hence it is important for everyone to understand the actual process of bunkering so here we go.

Pre-bunker preparations.

The most important aspect of bunkering operation is the “checklists”, which forms a part of company’s safety management system (SMS) and I.S.M.,eliminating the possibility and negligence of human and other operational errors. The pre-bunkering checklist must be followed in-consultation with the Chief Engineer (C/E), as he is the person-in-charge for the bunkering operation. Before bunkering, ususally it is 4th engineering officer, taking “soundings” of bunker tanks and calculates the volume of fuel oil available in every fuel oil tank of the ship. Then a Bunker-plan is made to plan the distribution of total quantity of bunker fuel oil.

Bunker Procurement

Ordering of Bunker oil:

The ship Managers (superintendents) monitor the performance of a fleet of ships. For eg. On owning a car, we tend to keep a check on its fuel consumption widely called as “mileage”. It is the distance travelled by the vehicle for a unit volume of fuel used. In the same way, as the ship consumes humungous quantity of fuel, whose costs are forming the major part of ship’s operation, The Managers tend to keep a check on it. This is measured in terms of specific fuel oil consumption of the main propulsion engine.

On knowing the fuel oil consumption for a day & next voyage plan, the quantity of fuel oil required is calculated and compared with the available bunker tank capacity. A requisition is placed through the C/E & Master of the vessel to the Managers. The requisition is processed and evaluated for the quality & quantity of fuel to be supplied for the particular ship. Planning is done for the delivery of bunker at a particular port where the oil is available at a comparitive lesser cost. On taking all these aspects into consideration, the Managers, deliver bunker to the vessel. Upon receiving the bunker, a sample collected during bunkering operation is sent for lab analysis to confirm the delivered oil meets the required standard for the safe & efficient operation of the auxiliary engines & main propulsion engine.

Pre-Bunker Checklist:

Pre-Bunkering Procedure:

  1. State of adjacent waters noticed
  2. Vessel properly secured to dock
  3. Check suppliers product corresponds to ordered product
  4. Agree quantity to be supplied
  5. Check valves open
  6. Day tanks full and supply valves closed
  7. Warning signs in position e.g. No Smoking
  8. SOPEP plan available
  9. Clean up material in place
  10. Oil Boom in place
  11. Foam fire extinguisher placed at bunker station
  12. Alfa Laval and transfer pumps off
  13. Fuel tank supply valves open
  14. Agree stop/start signals between vessel andbarge/truck
  15. Bravo flag flying/red light showing
  16. Agree pumping/transfer rate
  17. Agree emergency shut down procedure
  18. Specification sheet received
  19. Check hose and couplings are secure and in good order
  20. Fuel nozzle and hose secured to vessel
  21. Check barge/truck meters Reading:
  22. Check on board meters Reading:
  23. Bunker Valve open
  24. Unused manifold connections blanked off
  25. Master informed
  26. Signal pumping to commence

The above checklist has to be completely filled religiously by both the ship & barge personnels. Please move on to the next page by clicking below

SOPEP equipments

At the bunker manifold and wherever necessary, as per the ships SOPEP plan, the SOPEP equipments should be kept in immediate readiness in order to avoid oil spill/pollution during bunkering operation.

SOPEP- Shipboard Oil Pollution Emergency Plan.

The SOPEP Locker must have minimum of the below specified items:

  1. absorbent roll
  2. absorbent pads
  3. absorbent granules
  4. absorbent materials
  5. brooms
  6. shovels
  7. mops
  8. scoops
  9. empty receptacles (200 ltrs capacity)
  10. portable air driven pumps
  11. oil boom
  12. oil spill dispersants.

These items must be stowed in an easily accessible locker, clearly marked, and is to be brought on deck ready for immediate use, prior to all oil transfer operations.

During Bunkering Procedures:

During Bunkering checklist:

  1. Witness taking and sealing of 2 representative product samples
  2. Monitor fuel connections for leaks fuel flow and control tank levels
  3. Change over of tanks whenever necessary.
  4. Checking the rate at which bunkers are received.
  5. Checking the tightness/slackness of mooring ropes.
  6. Checking trim/list of the bunker barge & the ship.
  7. Continuous monitoring/look outs for the vessel’s position(when at anchor).

During bunkering, the above checklist must be filled up and continuous monitoring of the above secified items are required till the bunkering operation is complete.

After Bunkering Procedures:

On completion of the bunkering operations, with the ship-barge co-ordination, the line should be blown with air to make sure the line is not filled with oil. The after-bunker checklist is followed.

After Bunker Checklist:

  1. Bunker Valve closed
  2. Disconnect hose (drain before disconnecting)
  3. Check barge/truck meter Reading:
  4. Check ships meter Reading:
  5. Sign Bunker Delivery Receipt BDR No: (Bunker Delivery report/Note).
  6. Retain BDR with product sample
  7. SOPEP plan returned to bridge
  8. Clean up gear stowed / Oil boom returned
  9. Bravo Flag/Red light stowed/switched off
  10. Remove and pack away warning/safety signs
  11. Foam fire extinguisher placed back in correct location
  12. Complete Oil Record Book
  13. Master informed of completion
  14. Confirm in Oil Record Book Bunkering checklist completed

Quantity Calculation & Temperature-Density Correction:

After bunkering of various fuel oil tanks, the quantity in each bunkered tank must be calculated to cross-check whether the received quantity of oil matches the requisition. For calculating the quantity, “sounding” of the tanks which are “bunkered” must be taken. The “Density” of the fuel oil supplied vary from place to place. It also varies with the temperature. As a thumb rule, the density of fuel oil decreases with increase in temperature. So, when the oil is supplied at a higher temperature, then the volume of oil supplied is less than what is supplied at lesser temperature.

Oil Temperature —————————-Density ——————————- Volume Of Oil Supplied

Increases————————————–Decreases————————————Lesser

Decreases——————————— —Increases ————————————-More

Also the formula which is generally used for temperature-density correction is as follows:

MT= {(t1-15)*0.00065}*volume of oil in m^3.

where MT stands for metric tonnes.

t1 stands for temperature of oil in bunker tanks in degree celcius,

0.00065 is the correction factor,

volume of oil in m^3, is obtained from the sounding table.

Safeties:

General Safeties During Bunkering:

  • SOPEP locker,
  • Emergency shut-down arrangements,
  • Bunker line over-flow arrangements to overflow tank with audible & visual alarm,
  • Relief valve in the bunker line,
  • Containment trays.
  • Consistent & Continuous look outs.

BDN & Related IMO Regulations for Bunkering:

Bunker Delivery Note (BDN):
– Becomes a Statutory document
– Must be kept on board for 3 years for inspection and a copy may be taken for further examination by PSC.
– Must contain all data required by Appendix V
– Name and IMO number of vessel Port
– Date of Commencement of delivery
– Details of fuel oil supplier
– Product name, quantity , Density at 15 0C and Sulphur content % m/m
– A declaration that fuel supplied meets Regulation 14 and 18 requirements

 

Fuel Oil Sampling
– A sealed sample meeting the requirements in associated guidelines has to supplied to the ship by the bunker supplier
– For each individual BDN a sample has to be taken at the vessel’s bunker receiving manifold. (see procedure in associated guidelines) – ISM  Manuals.
– The sample label has to be signed by both the bunker supplier’s representative and the vessel’s Chief Engineer.
– The sample size shall be not less than 400 mls
– The sample is not to be used for any commercial purpose
– The sample is to be retained on board for at least 1 year for inspection by PSC as required

 

Shipboard Procedures for  BDN and Samples

  • Adequate bunker manifold location for sampler attachment
  • External safe storage location for samples for 1 year period
  • Log book for sample retention and custody transfer
  • Safe storage for BDNs and other documents relating to bunkering onboard
  • Port/Flag State Control Guidelines
  • Proposed Guidelines from FSI 13 for MEPC 53 approval.
  • Initial inspections and Primary survey parameters – then “Clear Grounds” for
  • in-depth inspections
  • “In depth” inspection parameters
  • Detainable deficiencies
  • Non-Party ship inspections

 Conclusion:

Thus bunkering operation is direclty related to “MARPOL” annexes, i.e annex 1 and annex 6. When oil is spilled it causes marine pollution under annex 1. When the bunkered oil doesn’t meet certain specifications, it causes pollution of air which comes under annex 6.

“MARPOL” will be dealt with in the future articles.

MARPOL Annex VI- Emissions Control Development

Introduction:

IMO ship pollution rules are contained in the “International Convention on the Prevention of Pollution from Ships”, known as MARPOL 73/78. On 27 September 1997, the MARPOL Convention has been amended by the “1997 Protocol”;, which includes Annex VI titled “Regulations for the Prevention of Air Pollution from Ships”. MARPOL Annex VI sets limits on NOx and SOx emissions from ship exhausts, and prohibits deliberate emissions of ozone depleting substances.

The IMO emission standards are commonly referred to as Tier I…III standards. The Tier I standards were defined in the 1997 version of Annex VI, while the Tier II/III standards were introduced by Annex VI amendments adopted in 2008, as follows:

  • 1997 Protocol (Tier I)—The “1997 Protocol” to MARPOL, which includes Annex VI, becomes effective 12 months after being accepted by 15 States with not less than 50% of world merchant shipping tonnage. On 18 May 2004, Samoa deposited its ratification as the 15th State (joining Bahamas, Bangladesh, Barbados, Denmark, Germany, Greece, Liberia, Marshal Islands, Norway, Panama, Singapore, Spain, Sweden, and Vanuatu). At that date, Annex VI was ratified by States with 54.57% of world merchant shipping tonnage.

Accordingly, Annex VI entered into force on 19 May 2005. It applies retroactively to new engines greater than 130 kW installed on vessels constructed on or after January 1, 2000, or which undergo a major conversion after that date. The regulation also applies to fixed and floating rigs and to drilling platforms (except for emissions associated directly with exploration and/or handling of sea-bed minerals). In anticipation of the Annex VI ratification, most marine engine manufacturers have been building engines compliant with the above standards since 2000.

  • 2008 Amendments (Tier II/III)—Annex VI amendments adopted in October 2008 introduced (1) new fuel quality requirements beginning from July 2010, (2) Tier II and III NOx emission standards for new engines, and (3) Tier I NOx requirements for existing pre-2000 engines.

The revised Annex VI enters into force on 1 July 2010. By October 2008, Annex VI was ratified by 53 countries (including the Unites States), representing 81.88% of tonnage.

Emission Control Areas:

Two sets of emission and fuel quality requirements are defined by Annex VI: (1) global requirements, and (2) more stringent requirements applicable to ships in Emission Control Areas (ECA). An Emission Control Area can be designated for SOx and PM, or NOx, or all three types of emissions from ships, subject to a proposal from a Party to Annex VI.

Existing Emission Control Areas include:

  • Baltic Sea (SOx, adopted: 1997 / entered into force: 2005)
  • North Sea (SOx, 2005/2006)
  • North American ECA, including most of US and Canadian coast (NOx & SOx, 2010/2012).
  • US Caribbean ECA, including Puerto Rico and the US Virgin Islands (NOx & SOx, 2011/2014).

Greenhouse Gas Emissions.

2011 Amendments to MARPOL Annex VI introduced mandatory measures to reduce emissions of greenhouse gases (GHG). The Amendments added a new Chapter 4 to Annex VI on “Regulations on energy efficiency for ships”.

NOx Emission Standards

NOx emission limits are set for diesel engines depending on the engine maximum operating speed (n, rpm), as shown in Table 1 and presented graphically in Figure 1. Tier I and Tier II limits are global, while the Tier III standards apply only in NOx Emission Control Areas.

Table 1. MARPOL Annex VI NOx Emission Limits
Tier Date NOx Limit, g/kWh
n < 130 130 ≤ n < 2000 n ≥ 2000
Tier I 2000 17.0 45 · n-0.2 9.8
Tier II 2011 14.4 44 · n-0.23 7.7
Tier III 2016† 3.4 9 · n-0.2 1.96
† In NOx Emission Control Areas (Tier II standards apply outside ECAs).

Figure 1. MARPOL Annex VI NOx Emission Limits

Tier II standards are expected to be met by combustion process optimization. The parameters examined by engine manufacturers include fuel injection timing, pressure, and rate (rate shaping), fuel nozzle flow area, exhaust valve timing, and cylinder compression volume.

Tier III standards are expected to require dedicated NOx emission control technologies such as various forms of water induction into the combustion process (with fuel, scavenging air, or in-cylinder), exhaust gas recirculation, or selective catalytic reduction.

Sulfur Content of Fuel

Annex VI regulations include caps on sulfur content of fuel oil as a measure to control SOx emissions and, indirectly, PM emissions (there are no explicit PM emission limits). Special fuel quality provisions exist for SOx Emission Control Areas (SOx ECA or SECA). The sulfur limits and implementation dates are listed in Table 2 and illustrated in Figure 2.

Table 2. MARPOL Annex VI Fuel Sulfur Limits
Date Sulfur Limit in Fuel (% m/m)
SOx ECA Global
2000 1.5% 4.5%
2010.07 1.0%
2012 3.5%
2015 0.1%
2020a 0.5%
a – alternative date is 2025, to be decided by a review in 2018

Figure 2. MARPOL Annex VI Fuel Sulfur Limits

Heavy fuel oil (HFO) is allowed provided it meets the applicable sulfur limit (i.e., there is no mandate to use distillate fuels).

Alternative measures are also allowed (in the SOx ECAs and globally) to reduce sulfur emissions, such as through the use of scrubbers. For example, in lieu of using the 1.5% S fuel in SOx ECAs, ships can fit an exhaust gas cleaning system or use any other technological method to limit SOx emissions to ≤ 6 g/kWh (as SO2).

Greenhouse Gas Emissions

MARPOL Annex VI, Chapter 4 introduces two mandatory mechanisms intended to ensure an energy efficiency standard for ships: (1) the Energy Efficiency Design Index (EEDI), for new ships, and (2) the Ship Energy Efficiency Management Plan (SEEMP) for all ships.

  • The EEDI is a performance-based mechanism that requires a certain minimum energy efficiency in new ships. Ship designers and builders are free to choose the technologies to satisfy the EEDI requirements in a specific ship design.
  • The SEEMP establishes a mechanism for operators to improve the energy efficiency of ships.

The regulations apply to all ships of and above 400 gross tonnage and enter into force from 1 January 2013. Flexibilities exist in the initial period of up to six and a half years after the entry into force, when the IMO may waive the requirement to comply with the EEDI for certain new ships, such as those that are already under construction.

 Ozone Depleting Substances:

Annex VI prohibits deliberate emissions of ozone depleting substances, which include halons and chlorofluorocarbons (CFCs). New installations containing ozone-depleting substances are prohibited on all ships. But new installations containing hydro-chlorofluorocarbons (HCFCs) are permitted until 1 January 2020.

Annex VI also prohibits the incineration on board ships of certain products, such as contaminated packaging materials and polychlorinated biphenyls (PCBs).

Compliance: Compliance with the provisions of Annex VI is determined by periodic inspections and surveys. Upon passing the surveys, the ship is issued an “International Air Pollution Prevention Certificate”, which is valid for up to 5 years. Under the “NOx Technical Code”, the ship operator (not the engine manufacturer) is responsible for in-use compliance.

This article based in part on information provided by Michael F. Pedersen of MAN Diesel A/S.

Chief Engineer’s Responsibilities of a ship in Dry-Dock

Drydocking is one of the most important activities that a vessel may come across. Hence a good planning and co-ordination will be vital towards successful completion of dry dock.
      

The dry docking is governed by various factors:-
1) Classification society requirement
2) Statutory requirement
3) Condition of vessel
So for a successful drydock there should be a good co-ordination between master and chief engineer so that all the works are completed at time without any casualty. 

 As a chief engineer following are the exchange of information which will be necessary with the master:-

1) Class, survey and statutory requirement
2) Scope of work in drydock categorizing especially time required, shore gang required, work that is to be done by engine room and dock staff.
3) ROB of bunkers and L.O. to be shared by master
4) Any requirement for pumping of black water, oil sludge to reception facilities and its arrangement.
5) Spare requirements as to what all spares have arrived and what will be arriving.
6) List of survey items to be submitted to master.
7) Any special requirement like covering of vents, opening of tanks when grit blasting is performed.
8) Co-ordination with master to required list and trim and put accordingly fuel oil and fresh water tanks in use as advised by him.
9) Communicate with master as to be in touch with company regarding any new requirements which ship will be fulfilling after dry dock. i.e. to fulfill any compliance towards statutory requirements.
10) Any rules laid down by yard should be informed to ship personnel by master.
11) A pre docking tank cleaning and line washing plan to be informed by master to chief engineer to mobilize the resources to carry out the operation.
12) All refit requirements to be submitted as stated with appropriate data e.g. pipe repair material, location, staging required etc.
13) If any changes to be made in the emergency teams in the dry dock should be well consulted before dry dock.

Delegation of responsibility to engine room staff:-
Preparedness for the same will start well in advance of the dry dock. The preparedness will include the following:-
1) How to change over main engine and boiler in diesel oil.
2) How to change the ship power to shore power taking in account of voltage and frequency.
3) Requirement of cooling of fridge and A/C plant
4) Method of sewage disposal.
5) Securing of heavy weights.
6) Tanks and coffer dams to be sounded.
7) Chief engineer and second engineer who are management level personnel of engine room department, to make a rough plan to delegate responsibility of various jobs.
8) Chief engineer will delegate responsibility for arranging spares as they arrive.
9) Personnel to prepare tags for various valves with job number and fix them on valve.
10) All safety aspects discussed and safety precautions to be followed. All engine room personnel to be briefed about safety and asked to check the shore personnel regarding safe working culture.
11) A day to day work report to be made and discussed to check whether all jobs are proceeding as per schedule or there is some delay. If same look into them.
12)  Chief engineer and second engineer to divide and co-ordinate various surveys which they will oversee.
Now while undocking of vessel there should be proper co-ordination between ship and yard personnel.

Various inspection and co-operation with dry dock personnel are:-
1) Check about the plan of dry dock and ensure that all works have been completed.
2) Check paint work has been completed.
3) Hull repair completed.
4) All tanks plugs are in place and secured.
5) All anodes are fitted. Grease/ paper used on them while painting, are removed.
6) Echo sounder transducer is cleaned of paper and grease.
7) Propeller rope guard is fitted properly and propellers are on dock mark.
8) Oil is not leaking from stern tube.
9) Rudder plugs are in place.
10) Ensure all valves are shut.
11) Sea grids are in place
12) Ensure all tanks are at same level while entry so as to have same trim when refloating
13) Verify weight log certificate ( no heavy weight has been shifted)

Duties of a C/E in dry dock:-

  1. To brief engine room staffs before docking and ensure they under stand their respective duties.
  2. Preparation of machinery survey in dry dock
  3. Preparation of dry dock list .
  4. Study previous dry dock reports and note clearance to be measured .
  5. Ensure all tools and spares are ready for use .
  6. Liaise with the shipyard manager and contractor to ensure correct works carried out .
  7. Emergency lightening and generator set to be tested before docking in case of shore power failure.
  8. Fire fighting equipments on board to be checked and tested and make ready for use .
  9. All tanks, wells and coffer dams to be sound and recorded.
  10. Minimum bunker and ballast to be carried.
  11. To ensure filter elements in oily water separator and renewed and system is checked and system is checked for satisfactory function.

“DEFINITONS AND SHIP DIMENSIONS”

“DEFINITONS AND SHIP DIMENSIONS”

Hull:

The structural body of a ship including shell plating, framing, decks and bulkheads.

Afterbody :

That portion of a ship’s hull abaft midships.

Forebody:

That portion of a ship’s hull forward midships.

Bow :

The forward of the ship

Stern :

The after end of the ship

Port :

The left side of the ship when looking forward

Starboard :

The right side of the ship when looking forward

After Perpendicular (AP):

A perpendicular drawn to the waterline at the point where the aft side of the rudder post meets the summer load line. Where no rudder post is fitted  it is taken as the centre line of the rudder stock.

Forward Perpendicular (FP):

A perpendicular drawn  to the waterline at the point  where  the foreside of the stem meets  the summer load line.

Length Between Perpendiculars (LBP):

The length between the forward and aft perpendiculars measured along the summer load line.

Amidships:

A point  midway between the after  and forward  perpendiculars.

Length Overall (LOA):

Length of vessel taken over all extremities.

Lloyd’s Length:  

Used  for  obtaining scantlings  if the  vessel  is classed  with Lloyd’s Register. It is the same as length  between perpendiculars except that it must not be less than  96 per cent and need  not be more  than  97 per cent of the extreme length  on the summer load line. If the ship has an unusual stem or stern arrangement the length  is given special consideration.

Register  Length:

It  is  the  length   of  ship  measured  from  the  fore-side  of the   head  of the stem to the aft side of the head  of the stern  post or, in the case of a ship not having a stern  post, to the fore-side of the rudder stock. If the  ship does  not  have a stern  post  or a rudder stock,  the  after  terminal is taken to  be  the  aftermost part  of the  transom or  stern  of the  ship.  This length  is the  official  length  in the  register of ships  maintained by the  flag state  and  appears on official  documents relating to ownership and  other matters  concerning the  business   of  the  ship.

IMO Length:

This length  is found  in various  international conventions such as the  Load  Line,  Tonnage and  SOLAS  conventions and  determines the  application of requirements of those conventions to a ship. It is defined as 96 per cent of the total length  on a waterline at 85 per  cent  of the  least  moulded depth measured from  the top  of keel,  or the  length  from  the  fore-side of stem  to the  axis of rudder stock on that waterline, if that  is greater.

Base Line:

A horizontal line drawn  at the top of the keel plate.  All vertical moulded dimensions are measured relative  to this line.

Moulded  Beam:

Measured at the midship  section  is the maximum  moulded breadth of the ship.

Moulded  Draft:

Measured from the base line to the summer load line at the midship  section.

Moulded  Depth:

Measured from the base line to the heel of the upper deck beam  at the ship’s side amidships.

Extreme Beam:

The maximum  beam  taken over all extremities.

Extreme Draft:

Taken  from the lowest point of keel to the summer load line. Draft  marks  represent extreme drafts.

Extreme  Depth:  

Depth of vessel  at  ship’s side  from  upper deck  to  lowest point  of keel.

Half  Breadth:  

Since  a  ship’s  hull  is  symmetrical about  the  longitudinal centre line, often  only the half beam  or half breadth at any section  is given.

Freeboard:

The  vertical  distance measured at  the  ship’s  side  between the summer load line (or service draft) and the freeboard deck.

Freeboard deck is normally  the uppermost complete deck exposed  to weather and sea which  has  permanent means  of closing  all openings, and  below  which  all openings in the ship’s side have watertight closings.

Sheer:

Curvature of decks in the longitudinal direction. Measured as the height  of deck at side at any point  above the height  of deck at side amid-ships.

Camber (or Round  of Beam):

Curvature of decks in the transverse direction. Measured as the height  of deck at centre above the height  of deck at side.

Rise of Floor (or Deadrise):

The  rise of the  bottom shell plating  line above the base line. This rise is measured at the line of moulded beam.

Half Siding of Keel:

The horizontal flat portion of the bottom shell measured to port  or starboard of the  ship’s longitudinal centre line. This is a useful dimension to know when dry-docking.

Tumblehome:

The  inward  curvature of the  side  shell  above  the  summer load line.

 Flare:

The outward curvature of the side shell above the waterline. It promotes dryness and is therefore associated with the fore end of ship.

Stem Rake:

Inclination of the stem line from the vertical.

 

Keel Rake:  

Inclination of the  keel  line  from  the  horizontal. Trawlers and tugs often  have keels raked  aft to give greater depth aft where the propeller diameter is proportionately larger  in this  type  of vessel. Small  craft  occa- sionally have forward  rake of keel to bring propellers above the line of keel.

TWEEN DECK HEIGHT:

Vertical distance between adjacent decks measured from the tops of deck beams  at ship side.

 

PARALLEL MIDDLE  BODY:

The  length  over  which  the  midship  section  remains constant in area  and shape.

ENTRANCE:  

The  immersed body of the  vessel forward  of the  parallel middle body.

RUN:

The immersed body of the vessel aft of the parallel middle  body.

TONNE PER CENTIMETRE (TPC)

It is the mass required to increase the mean draught by 1 centimetre.

 

LIGHT WEIGHT OR MASS

The weight of the ship, in tonne, complete and ready for sea but without crews, passengers, stores, fuel or cargo on board.

 

DEADWEIGHT

The difference between the displacement and the lightweight at any given draught, again measured in tonne. It is the weight of cargo, fuel, stores  etc.

 

TONNAGE MEASUREMENT

  • This is often referred to when the size of the vessel is discussed, and the gross tonnage is quoted from Lloyd’s register.
  • Tonnage is a measure of the enclosed internal volume of the vessel, 100 cubic feet representing one ton
  • Its normally divided into categories as follow:-

Displacement Tonnage

  • A ship’s displacement is the sum of the ship’s actual weight (lightweight) and it’s contents (deadweight).
  • The metric unit of measurement is 1 tonne (= 1000 Kg).
  • The displacement represents the amount of water displaced by the ship expressed in tonnes.
  • The weight of water displaced therefore equals the weight of the ship

 

TONNE PER CENTIMETRE (TPC)
          It is the mass required to increase the mean draught by 1 centimetre.

LOAD DISPLACEMENT
          The weight of the ship and its content, measured in tonne. The value will vary according to the ship’s draught.

DEADWEIGHT SCALE
          It is a scale diagram indicating the deadweight of the ship at various draughts.

 

FORM COEFFICIENT
          It is devised to show the relationship between the form of  the ship and the dimension of the ship.

 

Lightweight Tonnage

  • The lightweight is the weight of the ship as built (hull, machinery) including boiler water, lubricating oil and the cooling water system.
  • Lightweight like displacement is expressed in units of tones.
  • It assumes importance in a commercial sense only when considering the value of the vessel which is to be broken up for scrape.

 

Deadweight tonnage (DWT)

  • Deadweight is the weight of the cargo which a ship carries plus weights of fuel, stores, water ballast, fresh water, crew and passengers and baggage.
  • It is the difference between the loaded ship displacement and the lightweight.

 

Gross Tonnage (GT)

  • Measurement of total internal volume of a vessel and includes all under deck tonnage and all enclosed spaces above tonnage deck.
  • 100 cubic feet of space being considered as 1 ton

 

Nett Tonnage (NT)

  • Ship measurement derived from gross tonnage by deducting spaces allowed for crew and propelling power.
  • 100 cubic feet of space being reckoned as 1 ton

 

LOAD LINE

The marking on the ship side that relate to the loading condition of the ship termed as the load line mark.

 

LOAD DISPLACEMENT

The weight of the ship and its content, measured in tonne. The value will vary according to the ship’s draught.

DEADWEIGHT SCALE

It is a scale diagram indicating the deadweight of the ship at various draughts.

FORM COEFFICIENT

It is devised to show the relationship between the form of  the ship and the dimension of the ship.

SCANTLING

The dimensions of the structural items of a ship, e.g. frames, girders, plating , etc.

 

INTERCOSTAL

Composed of separate parts, non-continuous.

“Surveys of Mechant Ships”

SURVEYS- AN OVERVIEW OF REQUIREMENTS AND CERTIFICATION

 

 

Period of certificate of class

 

The period of the certificate of class starts either from the date of initial classification or from the credited date of the last class renewal/special survey, and expires at the due date assigned for the next class renewal/special survey.

The due date is the end of the time window for that survey.

Anniversary date

The anniversary date is the day and the month given in the certificate of class which corresponds to the expiry date of the certificate.

Survey time window

The survey time window is the fixed period during which the annual and intermediate surveys are to be carried out.

Overdue surveys

Each periodical survey is assigned a due date specified by the relevant Rules by which it is to be completed.

A survey becomes overdue when it has not been completed by its due date. For example, with an anniversary date of 15th April, the annual survey can be validly carried out from 16th January to 15th July. If not completed by 15th July, the annual survey becomes overdue and class will be suspended automatically.

Recommendations/Conditions of Class

‘Recommendation’ and ‘Condition of Class’ are different terms used by IACS Societies for the same thing, i.e. requirements to the effect that specific measures, repairs, surveys etc. are to be carried out within a specific time limit in order to retain class.

Memoranda

Other information of assistance to the surveyor and owners may be recorded as ‘memoranda’ or a similar term. They may, for example, include notes concerning materials and other constructional information. A memorandum may also define a condition which, though deviating from the technical standard, does not affect the class (e.g. slight indents in the shell which do not have an effect upon the overall strength of the hull or minor deficiencies, which do not affect the operational safety of the machinery).

In addition, memoranda could define recurring survey requirements, such as annual survey of specified spaces, or retrofit requirements, which have the de-facto effect of conditions of class.

Specific questions in relation to the meaning of memoranda / recommendations / conditions of class are to be addressed to the Classification Society concerned though the owner of the ship.

Class surveys periodicity and scope

Class renewal survey / special survey

Class renewal surveys/special surveys are carried out at five-year intervals. However, consideration may be given by the Society, in exceptional circumstances, to granting an extension for a maximum period of three months after the due date. In such cases the next period of class will start from the due date for the previous class renewal survey before the extension was granted.

The special survey may be commenced at the 4th annual survey and be progressed with a view to completion by the 5th anniversary date.

The class renewal surveys/special surveys include extensive examinations to verify that the structure, main and essential auxiliary machinery, systems and equipment of the ship are in a condition which satisfies the relevant Rules. The examinations of the hull are generally supplemented by thickness measurements and witnessing of tests as specified in the Rules, and as deemed necessary by the attending surveyor, to assess that the structural condition remains effective and to help identify substantial corrosion, significant deformation, fractures, damages or other structural deterioration.

Annual survey

Annual surveys are to be carried out within a window from three months before to three months after each anniversary date.

At the time of annual surveys, the ship is generally examined. The survey includes an inspection of the hull, equipment and machinery of the ship and some witnessing of tests, so far as is necessary and practical in order to verify that, in the opinion of the attending surveyor(s) the ship is in a general condition which satisfies the Rule requirements.

Intermediate survey

An intermediate survey is to be carried out within the window from three months before the second to three months after the third anniversary date.

The intermediate survey includes examinations and checks on the structure as specified in the Rules to verify that the vessel is in compliance with the applicable Rule requirements. The Rule criteria become more stringent with age.

According to the type and age of the ship the examinations of the hull may be supplemented by thickness measurements as specified in the Rules and where deemed necessary by the attending surveyor.

Bottom / Docking survey

A bottom/docking survey is the examination of the outside of the ship’s hull and related items.

This examination may be carried out with the ship either in dry dock (or on a slipway) or afloat: in the former case the survey will be referred to as dry- docking survey, while in the latter case as in-water survey. The conditions for acceptance of an in-water survey in lieu of a dry-docking survey will depend on the type and age of the ship and the previous history.

The outside of the ship’s hull and related items are to be examined on two occasions in the five-year period of the certificate of class with a maximum of 36 months between surveys.

One of the two bottom/docking surveys to be performed in the five-year period is to be concurrent with the class renewal/special survey.

For ships subject to the Enhanced Survey Programme (ESP) and 15 years of age and above, the intermediate bottom/docking survey is to be carried out in a dry-dock.

Tailshaft  survey

A tailshaft survey is the survey of screw shafts and tube shafts (hereafter referred to as tailshafts) and the stern bearing.

The different types of surveys to which tailshafts may be subjected and the intervals are:

  • complete survey;
  • modified survey;
  • Partial survey.

Tailshaft complete survey

Tailshafts are to be submitted to complete examination at a periodicity based on the type of shaft and its design. “Complete” means that the shaft is drawn up for examination or that other equivalent means of examination are provided.

Tailshaft modified survey

A modified survey of the tailshaft is an examination which may be accepted at alternate five-yearly surveys for tailshafts provided that the shaft arrangement is in accordance with specific requirements.

 

Tailshaft partial survey

A partial survey allows a postponement of the complete survey, having a periodicity of 5 years, for 2.5 years.

Boiler surveys

Boilers and thermal oil heaters are to be surveyed twice in every five-year period. The periodicity of the boiler survey is normally 2.5 years.

Steam boilers, superheaters and economisers are examined internally and externally. To this end, boilers are to be drained and suitably prepared for the examination of the water- steam side and the fire side. Where necessary, the external surfaces are to be made accessible for inspection by removal of insulation and lining.

Non-periodical surveys

Such surveys are carried out for example:

  • to update classification documents (e.g. change of owner, name of the ship, change of flag);
  • to deal with damage or suspected damage, repair or renewal work, alterations or conversion, postponement of surveys or outstanding recommendations/conditions of class;
  • At the time of port State control inspections.

In the event of damage which affects or may affect the class of the ship, the owner is to advise the Society without delay.

Arrangements are then made at the earliest opportunity for a surveyor to attend and ascertain the extent of the damage and determine if it is such that the vessel no longer complies with the applicable Rule requirements.

Following repair, the surveyor will again assess the status of the vessel to determine if it has been returned to a condition that is in compliance with the applicable Rule requirements.

Any damage in association with wastage over the allowable limits (including buckling, grooving, detachment or fracture), or extensive areas of wastage over the allowable limits, which affects or, in the opinion of the surveyor, will affect the vessel’s structural, watertight or weathertight integrity, is to be promptly and thoroughly repaired thereby removing the need for the imposition of any associated condition of classification. Otherwise, damages and partial or temporary repairs considered acceptable by the surveyor for a limited period of time are covered by the issuance of an appropriate recommendation/condition of class.

Damages or repairs required by the surveyor to be re-examined after a certain period of time are also covered by an appropriate recommendation/condition of class.

Class certificate

Issue of the certificate of classification

A certificate of classification, bearing the class notations assigned to the ship and an expiry date, is issued to all classed ships. This certificate may also be provided with annexes supplying information sufficient for the management of the certificate, for determining the class surveys date and for immediate assessment of possible irregularities (overdue recommendations, etc.).

An interim/provisional certificate of classification may serve as a certificate of classification in certain situations when deemed necessary by the Society.

Validity of the certificate of classification

A certificate of classification, properly endorsed, is valid until the expiry date unless advised otherwise by the Society or provided there are no grounds for suspension or withdrawal of class.

Endorsement of the certificate of classification

When annual and intermediate surveys are satisfactorily completed, the certificate of classification is:

  • endorsed for the periodical surveys;
  • according to the practice of some Societies, endorsed accordingly with the relevant entries in the appropriate annexes attached to the certificate concerning the outstanding recommendations/conditions of class, if any, and/or the surveys held.

Where applicable, memoranda are also endorsed in the appropriate annex.

Definitions and procedures related to statutory surveys and inspections

General

A number of the Conventions require an initial survey before a vessel is put in service for the first time and receives its first certificate, and a certificate renewal survey at one, two or five year intervals thereafter, depending on the certificate and type of ship. In addition, for those certificates valid for more than one year, surveys at annual intervals are required, one of which, at approximately half way and termed ‘intermediate’, may be of greater extent than an ordinary ‘annual’. The ‘Harmonized System of Survey and Certification’ (HSSC) implemented by many Administrations under IMO resolution A.997(25), as amended, brings all SOLAS (except for passenger ships), MARPOL and Load Line Convention surveys into a five-year cycle. With respect of safety equipment surveys, HSSC uses the term ‘periodical’ instead of ‘intermediate’, and for radio, ‘periodical’ instead of ‘annual’. These latter take the place of the renewal surveys held under the shorter certificate renewal cycles.

The scope of survey can generally be harmonized with the extents of the classification surveys detailed above and, as far as possible, are held concurrently with them.

The scope of each statutory survey or inspection is laid down by IMO resolutions and generally increases with age. It is to include sufficiently extensive examinations and checks to verify that the structure, machinery,

Systems and relevant equipment such as the life saving, fire fighting or pollution prevention equipment are in a

Satisfactory condition and in compliance with the applicable standards.

Between surveys, the Conventions require the flag Administration to make it compulsory for the owner to maintain the ship in conformance with the regulations so that the ship will remain fit to proceed to sea without danger to the ship or persons on board or unreasonable threat of harm to the marine environment.

Initial statutory survey

An initial survey is an inspection of the design and construction of the relevant structure, machinery and equipment of the ship to verify that it complies with the requirements of the applicable regulations.

 

Renewal statutory survey

A renewal survey is an inspection of the structure, machinery and/or equipment, as applicable, to verify that their condition is in compliance with the requirements of the regulations. Modifications to the ship having a bearing on the conformity of the vessel to the requirements are to be declared by the owner and inspected.

Annual statutory survey

An annual survey, in principle, includes a general inspection of the relevant structure and equipment of the ship to confirm that it has been maintained in accordance with the regulations and is in satisfactory condition.

Intermediate statutory survey

An intermediate survey is an inspection of specified items relevant to the particular certificate to confirm that they are in satisfactory condition. Depending on the certificate concerned and the age of the ship, the scope may range from that of an annual to the equivalent of a renewal survey.

Periodical statutory survey

Periodical surveys generally take the place of renewal surveys for those certificates which previously were renewed after one or two years. However, in the case of a Load Line Certificate which is issued on behalf of, or by, flag Administrations that have not implemented the harmonized system of survey and certification, the five-year renewal survey may be referred to as the ‘periodical’ survey.

 Statutory certificates

Authorization

Statutory certificates are issued by the RO in accordance with the terms of its recognition by the flag Administration. Variation of the delegation of statutory authority or certificates that can be issued by the RO exists between Administrations. The Administration should be contacted for specific details of the authorization.

Issue, endorsement and withdrawal

A certificate is issued or endorsed after the relevant surveys are passed. A certificate may be issued, valid for a short time period, listing corrective action to be rectified for minor deficiencies which do not prevent the issuance of a certificate to the ship.

For most Conventions, the Administration empowers the RO to withdraw or invalidate a certificate if the required corrective action is not taken.

ASSIGNMENT, MAINTENANCE, SUSPENSION AND WITHDRAWAL OF CLASS

Assignment of class

Class is assigned to a ship upon the completion of satisfactory surveys, held to verify that the vessel is in compliance with the relevant Rules of the Society. This assignment may be given in the following cases:

  • On completion of the new building, after satisfactory surveys have been performed;
  • on completion of a satisfactory survey of an existing ship carried out in accordance with the agreement developed by the IACS Member Societies for ships transferring class between Members; or
  • On completion of a satisfactory specific class survey of an existing ship not classed with an IACS Society, or not classed at all.

Maintenance of class

Classed ships are subject to surveys for maintenance of class. These surveys include the class renewal (also called “special survey”), intermediate, annual, and bottom/docking surveys (either a survey in dry dock or an in-water survey) of the hull, tailshaft survey, boiler survey, machinery surveys and surveys for the maintenance of additional class notations, where applicable. Such surveys are carried out at the intervals and under the conditions given below.

The surveys are to be carried out in accordance with the relevant requirements in order to confirm that the condition of the hull, machinery, equipment and appliances comply with the applicable Rules. It is the owner’s duty to ensure that the ship’s maintenance is kept at a satisfactory level in order to maintain the condition between surveys.

The extent of any survey depends upon the condition of the ship and its equipment. In addition to the minimum required extent of surveys specified in the Rules, should the surveyor have a doubt as to the maintenance or condition of the ship or its equipment, or be informed by the owner of any deficiency or damage which may affect class, further examination and testing may be conducted as considered necessary.

Suspension of class

Class may be suspended following a decision made by the Society when one or more of the following occurs:

  • When a ship is not operated in compliance with the Rule requirements;
  • When a ship proceeds to sea with less freeboard than that assigned;
  • When the owner fails to request a survey after having detected defects or damages affecting the class;
  • When repairs, alterations or conversions affecting the class are carried out without requesting the attendance of a surveyor.

In addition, class is automatically suspended:

  • when the class renewal/special survey has not been completed by its due date or within the time granted in special circumstances for the completion of the survey, unless the ship is under attendance by the Society’s surveyor(s) with a view to completion prior to resuming trading;
  • When the annual or intermediate surveys have not been completed by the end of the corresponding survey time windows.

Suspension of class with respect to the above cases will remain in effect until such time as the due surveys and any other survey deemed appropriate by the Society have been completed.

In addition to the circumstances for which automatic suspension may apply, the class of a ship will be subject to suspension procedures following a decision of the Society:

  • when a recommendation/condition of class is not dealt with within the time limit specified, unless it is postponed before the due date by agreement with the Society;
  • When one or more other surveys are not held by their due dates – or the dates stipulated by the Society also taking into account any extensions granted;
  • When, due to the nature of reported defects, the Society considers that a ship is not entitled to retain its class even on a temporary basis (pending necessary repairs or renewals, etc.);
  • In other circumstances where the owner fails to submit the ship to a survey in accordance with a special requirement.

In all cases suspension will remain in effect until such time as matters are rectified and the class is reinstated or class is withdrawn.

Depending on the Society’s procedures, the suspensions of class which are not automatic may take effect either when they are decided by the Society or from the date when the conditions for suspension occurred. However once the conditions for class suspension/withdrawal are met and before any decision by the Society can be taken, either because the Society is not aware of the circumstances (surveys dates, etc. are recorded but not systematically monitored) or because the decision is not yet taken, maintenance of class cannot generally be confirmed by the Society during this period.

Withdrawal of class

The Society will withdraw the class of a ship when:

  • requested by the owner;
  • The class has been suspended for more than six months;
  • The ship is reported as a constructive total loss and the owner does not advise his intention to repair the ship for re-instatement of class;
  • The ship is reported lost;
  • The ship will not trade further as declared by its owner.

Withdrawal of class takes effect from the date on which the circumstances causing such withdrawal occur or when it is decided.

Notification of suspension or withdrawal

When class is suspended or withdrawn, the Society will at the same time:

  • inform the owner, flag Administration and underwriters (the latter at their request);
  • publish the information on its website and convey the information to appropriate databases (Equasis, etc.).
Certificate Index
Registry
Certificate of Registry
Indefinitely Valid
Statutory
International Load Line
5 Years
All Ships. Required Under Loadline convention. Subject to Annual Endorsement. International Load Line Exemption Certificate must be carried were exemptions under Loadline 1988 protocol applies
IOPP
5 Years
All tankers above 150GRT and all other ships above 400GRT. Required under MARPOL 73/78. Subject to Annual and intermediate Endorsements. The certificate is supplemented by a Record of Construction and Equipment for ships other than Oil Tankers (Form A) or a Record of Construction for Oil Tankers (Form B)
Cargo Ship Safety Construction Certificate
5 Years
All Cargo ships over 500GRT.SOLAS Requirement. Supplemented by Record of Construction and Equipment. Subject to Annual and intermediate Endorsements
Passenger Ships Safety Certificate
1 Year
All Passenger vessels. SOLAS Requirement. Supplemented by Record of Equipment. Associated to this may be an Exemption Certificate, Special Trade Passenger Ship Certificate, Special Trade Passenger Ships Space Certificate as well as Search and Rescue Co-operation plan, List of operational limitations and Decision Support System for Masters
Cargo Ship Safety Equipment certificate
2 Years
All Cargo ships over 500GRT. Supplemented by Record of Equipment. Subject to Annual and intermediate Endorsements
Safety Radio Certificate
1 Year
SOLAS Requirement. All Cargo ships over 300GRT.
Dangerous Goods Manifest
per Voyage
SOLAS/MARPOL. Any vessel carrying dangerous goods.
Documentation of authorization for Carriage of Grain
Indefinitely Valid
Issued to every vessel loaded in accordance with International Code for the Safe Carriage of Grain in Bulk
Document of Compliance for Ships Carrying Dangerous Goods
5 Years
SOLAS. Document giving evidence that construction and equipment is appropriate to goods carried.
Noxious Liquid Substances
5 Years
Subject to Annual and intermediate Endorsements. MARPOL.
SOPEP Manual
Approved by administration
MARPOL. Every oil tanker over 150GRT and every ship over 400GRT
US Coast Guard Letter of Compliance
2 Years
Annual Inspections
ISM
Document of Compliance
5 Years
Subject to Annual and intermediate Endorsements. SOLAS
Safety management Certificate
5 Years
Subject to intermediate survey
Marine management Agreement
Class
Cargo Securing Manual
Class Approved. All Ships carrying cargos other than solid and liquid bulk .SOLAS.
Class Automation
5 Years
Classification Certificate:
5 Years
Subject to Annual, intermediate , Continuous (CSH) and Special Surveys
Classification Certificate: Hull
5 Years
Subject to Annual, intermediate , Continuous (CSH) and Special Surveys
Classification Certificate: Machinery
5 Years
Subject to Annual, intermediate , Continuous (CSM) and Special Surveys
Classification Certificate: Refrigeration
5 Years
Subject to Annual, intermediate , Continuous and Special Surveys
Dry-Docking
5 Years
Intermediate to be held between 2nd and 3rd anniversary dates.
In- Water Surveys
Special case survey which may replace intermediate docking under certain circumstances
Exhaust Gas Boiler
5 Years
Intermediate to be held between 2nd and 3rd anniversary dates.
Inert gas Plant
5 Years
Oil Fired Boiler
5 Years
Intermediate to be held between 2nd and 3rd anniversary dates.
TailShaft
5 Years
Hull Thickness Measurements
5 Years
Special surveys 1st to 5th Special surveys
Documents
Intact Stability
Every passenger ship and every cargo ship over 24m.
Damage Control Booklets
For all passenger and Cargo Ships. Plans showing watertight boundaries, compartments etc
Minimum Safe manning Document
Certificates for Masters, Officers and Ratings
STCW 95
Oil Record Book
Every Oil Tanker over 150GRT and every ship over 400GRT must have Part 1, Oil tankers over 150GRT must have part 2
Garbage management Plan
Every ship over 400GRT and every ship carrying 15 persons
Garbage Record Book
Every ship over 400GRT and every ship carrying 15 persons
Document of Compliance with the requirements for ships carrying dangerous goods
A suitable document giving evidence of construction and design
Certificate of Insurance or other financial security in respect of civil liability for oil pollution damage
Each ship carrying 2000tons or more of oil in bulk
Enhanced Survey Report File
Bulkers and tankers
Record of Oil Discharge Monitoring and control system for last ballast voyage
MARPOL Requirement. Record of oil content in any continuous discharge
Bulk Carrier Booklet
To prevent over stressing of hull
Cargo Record Book
Every ship to which Annex II applies of MARPOL,
International Pollution Prevention Certificate for the Carriage of Noxious liquid Substances in Bulk
Including certificates under Bulk Chemical Code
Procedures and Arrangements Manual
Every ship certified to carry Noxious liquid substances in bulk
Certificate of Fitness for the Carriage of dangerous chemicals in Bulk
Mandatory under Annex II
Certificate of Fitness to carry Liquid Gasses in Bulk

“Lubricants and Fuel Properties”

Types of lubrication

Hydrostatic Lubrication

If one examines the requirements of lubrication among the large number of moving parts in a diesel engine, it will be noticed that the working conditions are varied widely. Different types are used depending on their use and components of the engine.

 

  • A Necessary Function

All material surfaces, no matter how smooth they are, show many irregularities in the form of peaks and valleys, which are large when considered on a molecular scale.

When these two solid surfaces are pressed over or slide over each other, a real contact between these surfaces occurs that will cause friction and consequently the production of heat. During the motion of the sliding surfaces, a considerable amount of frictional heat is evolved at the rubbing surface. This results in high local temperature even under relatively light loads and speeds. This friction also causes a lot of wear and tear of the surfaces of the moving parts.

Even under small load, the local pressure at the peaks of the metals may be sufficiently great to cause appreciable deformation in ductile metals. If two materials of different hardness slide over one another, the peaks of the softer metal get broken more easily than the peaks of the harder metals.

Lubrication reduces friction between the moving surfaces or rolling pairs. The lubricant also acts as a coolant carrying heat away from the sliding surfaces, so proper lubrication of all the moving parts is an important function in machinery or engine operation. By lubrication we keep the moving surfaces separated by a fluid of some defined property.

Lubrication system is very important in diesel engines. Lubrication reduces friction between the moving surfaces or rolling pairs. various types of lubrication like hydrodynamic lubrication, hydrostatic lubrication, boundary lubrication which are used in diesel engines are explained in this article

  • Types of Lubrication

Considering the nature of motion between moving or sliding surfaces, there are different types of mechanisms by which the lubrication is done. They are:

  • Hydrodynamic lubrication or thick film lubrication
  • Hydrostatic lubrication
  • Boundary lubrication or thin film lubrication
  • Extreme pressure lubrication

Hydrodynamic Lubrication or Thick Film Lubrication

Hydrodynamic lubrication is said to exist when the moving surfaces are separated by the pressure of a continuous unbroken film or layer of lubrication. In this type of lubrication, the load is taken completely by the oil film.

The basis of hydrodynamic lubrication is the formation of an oil wedge. When the journal rotates, it creates an oil taper or wedge between the two surfaces, and the pressure build up with the oil film supports the load.

Hydrodynamic lubrication depends on:

  • relative speed between the surfaces,
  • oil viscosity,
  • load, and
  • clearance between the moving or sliding surfaces.

In hydrodynamic lubrication the lube oil film thickness is greater than outlet, pressure at the inlet increases quickly, remains fairly steady having a maximum value a little to the outside of the bearing center line, and then decreases quickly to zero at the outlet.

Application of hydrodynamic lubrication

  • Delicate instruments.
  • Scientific instruments.
  • Large plain bearings like pedestal bearings, main bearing of diesel engines.

Fig: Hydrodynamic Lubrication

  • Elastohydrodynamic

This is the type of lubrication used with rolling element bearings. To clarify, the material of the running surface deforms under high pressure as the rolling element passes over it. The oil wedge forms in this deformation.

(i) Deformation and increased viscosity with pressure are involved

(ii) Frictional coefficient = 0.05

(iii) film thickness less than Hydrodynamic

  • Hydrostatic Lubrication

Hydrostatic lubrication is essentially a form of hydrodynamic lubrication in which the metal surfaces are separated by a complete film of oil, but instead of being self-generated, the separating pressure is supplied by an external oil pump.

Hydrostatic lubrication depends on the inlet pressure of lube oil and clearance between the metal surfaces, whereas

hydrodynamic lubrication it depends on the relative speed between the surfaces, oil viscosity, load on the surfaces, and clearance between the moving surfaces.

Example: the cross head pin bearing or gudgeon pin bearing in two stroke engines employs this hydrostatic lubrication mechanism. In the cross head bearing, the load is very high and the motion is not continuous as the bearing oscillation is fairly short. Thus hydrodynamic lubrication cannot be achieved. Under such conditions, hydrostatic lubrication offers the advantage.

Hydrostatic Lubrication

  • Boundary Lubrication or Thin Film Lubrication

Boundary lubrication exists when the operating condition are such that it is not possible to establish a full fluid condition, particularly at low relative speeds between the moving or sliding surfaces.

The oil film thickness may be reduced to such a degree that metal to metal contact occurs between the moving surfaces. The oil film thickness is so small that oiliness becomes predominant for boundary lubrication.

Boundary lubrication happens when

  • A shaft starts moving from rest.
  • The speed is very low.
  • The load is very high.
  • Viscosity of the lubricant is too low.

Examples for boundary lubrication:

  • Guide and guide shoe in two stroke engine.
  • Lubrication of the journal bearing in diesel engines (mainly during starting and stopping of engine).
  • Piston rings and when cylinder liner is at TDC and BDC position when the piston direction changes and if the relative speed is very slow.

  • Boundary Lubrication
  • Extreme Pressure Lubrication

When the moving or sliding surfaces are under very high pressure and speed, a high local temperature is attained. Under such condition, liquid lubricant fails to stick to the moving parts and may decompose and even vaporize. To meet this extreme pressure condition, special additives are added to the minerals oils. These are called “extreme pressure lubrication.” These additives form on the metal surfaces more durable films capable of withstanding high loads and high temperature. Additives are organic compounds like chlorine (as in chlorinated esters), sulphur (as in sulphurized oils), and phosphorus (as in tricresyl phosphate).

distribution within a journal bearing

If the maximum radial clearance is Cr

then Cr = e + Hm

where is the eccentricity between the shaft and bearing centreline and Hm is the minimum clearance (oil film thickness)

an eccentricity factor can be calculated from

n = e / Cr

Factors involved with the eccentricity factor n are; minimum oil film thickness, journal attitude angle, pressure distribution, peak pressure angle, friction, horsepower loss and oil flow through the loaded region. The latter three determine the temperature of the bearing which for high speed bearings can be a limiting factor.

Lube Oil requirements for Diesel Engines

Crankcase

The oil has to serve two purposes;

  1. reduce friction
  2. Cool bearings

A good quality mineral oil will serve the purpose of reducing friction to an acceptable level depending upon the metals involved and other conditions such as temperature. All oils will oxidise and this reduces its effectiveness as a lubricant. Oxidation will also cause deposits which can block passage ways and coat working parts. The rate of oxidation will depend upon temperature, the higher the temperature the more rapid the rate. Anti oxidants are available which reduce the rate, also additional properties can be achieved by the use of additives.

Under high temperatures an oil is liable to thermal degradation which causes discoloration and changes the viscosity. Additives cannot change an oils susceptibility to this degradation. The refining process can remove compounds which effect the thermal stability of the oil and also those that lower oxidation resistance. Most of the chemicals found in an oil will react more or less with oxygen, The effects of this oxidation is always undesirable. Hence, a major objective of the refining process of a mineral oil is to remove those hydrocarbons i.e. the aromatics, the small amount of unsaturates together with molecules containing sulphur, oxygen and nitrogen.

Unfortunately these same molecules are those that improve the boundary lubrication performance. Hence, a careful balance must be struck. The use of anti-oxidants make a slightly better balance although there usefulness is limited.

Tin based white metal is susceptible to hardening as an oxide layers from on the surface.

These tin oxides are a grey-black in appearance and are extremely hard. There formation reduces the bearing clearance as the oxide layer is thicker than the original white metal material from which it formed. The oxide has a lower coefficient of friction than the original white metal but it will cause problems if it brakes up as fragments will become embedded edge on in the white metal and can score the pin.

Contamination

Water

 

Water from,

  1. bilge’s
  2. Jackets
  3. Sea via coolers
  4. leaky seals or washing in purifiers
  5. Condensation

Problems caused by water contamination,

    • Water leads to corrosion especially if there is sulphur present due to fuel contamination
    • forms emulsions which are not capable of withstanding high loads
    • removes water soluble additives when centrifuged out
    • leads to possible bacterial attack

Fuel

May be heavy residual or light diesel/gas oil and can be sourced to faulty to cylinder combustion or faulty seals on fuel p/ps.

Problems

    • Increases viscosity for hfo, reduces viscosity for D.O.
    • reduces flashpoint
    • Introduces impurities such as sulphur
    • dilutes lub oil when in large quantities

Solid impurities

  • carbon from the cylinder combustion process, particularly of importance with trunk piston engines but also for crosshead engines with inefficient diaphragm. The carbon can lead to restrictions and blockages of oil ways causing bearing failure. Straight mineral oils hold 1% carbon in suspension, dispersant oils hold about 5%.

Bacterial attack

Certain bacteria will attack oil but water must be present. The bacteria may exist in a dormant state in the oil but water is required if they are to reproduce.. The bacteria digest the oil causing breakdown emulsions to be formed, acidity increases, dead bacteria block filters and corrosive films form on working surfaces.

In summary their must be three essential conditions for microbiological growth;

    • There must be a source of carbon- present in the oil
    • There must be some bacteria or fungal spores present-these are almost universally present in the atmosphere
    • There must be free water present

Two other factors which encourage the growth are a slight acidity in the water (pH 5 or 6) and a slightly raised temperature (20 to 40oC) which can lead to rapid growth.

Biocide additives are available but they are not always compatible with other desired additives and can lead to large organic blockages if treated in the machinery. The best solution is to avoid the presence of water. If mild attack takes place the oil may be heated in the renovating tank to above 90oC for 24hrs before being returned to the sump via the centrifugal separator. For a severe attack the only solution is complete replacement of the charge followed by sterilisation of the system. It may be noted that on replenishment the bacteria may be present in a dormant state in the new charge.

Test results of crankcase oils

Viscosity-Increases due to thermal degradation or hfo contamination, reduces with diesel oil contamination, corrective action needed if it increases by 25% from new oil.

Water content-Corrective action required at 1%

Insoluble Sediments-basically the result of wear and oxidation, corrective action at 1% by weight

Ash-a measure of incombustibles in the oil sample, corrective action at 0.13% by weight

TAN-Total acid number consists of the strong acids (mainly sulphuric acid) formed in the combustion process and weak acids resulting form oxidation of the lub oil.

SAN-Strong acid number, the oil should be renewed if any is detected

TBN-Total base number indicates the alkaline reserve particulary important for trunk piston engines

Closed flash point-highlightd fuel contamination, corrective action if reduces by 30oC from new

Cylinder lub oil

The type of cyl l.o. required will depend upon the cylinder conditions and the engine design e.g crosshead or trunk piston. However, the property requirements are basically the same but will vary in degree depending upon the fuel and operating conditions.

 

Normal properties required are;

  1. adequate viscosity at working temperature so that the oil spreads over the liner surface to provide a tough film which resists the scrapper action of the piston rings
  2. the oil must provide an effective seal between the rings and liner
  3. only a soft deposit must be formed when the oil burns
  4. alkalintiy level (total base number or TBN) must match the acidity of the oil being burnt
  5. detergent and dispersant properties are required in order to hold deposits in suspension and thus keep surfaces clean

Additives

All oils for all purposes can be designed to give particular properties through the careful use of additives to the base mineral oil stock.

 

Common additives are;

    • Antioxidants– these are used in all oils to reduce the rate at which oxidation occurs and are especially useful were the lub oil cools the piston
    • Extreme pressure agents – these are compounds of phosphorus, Sulphur or Chlorine which increase the strength of the oil film under conditions of high temperature or pressure.
    • ,Dispersants or detergents– found in trunk piston engine oils and cyl l.o. these keep surfaces clean/ wash by holding deposits in suspension.
    • Viscosity index improvers–  these prevent excessive changes in viscosity with change in temperature
    • Other additives can be defined by name such as anti-wearanti-corrosionanti-bacteriaanti-foaming etc.

When running in, the cylinder lube oil injector pumps may be filled with a a straight mineral oil without anti-wear properties- typically the crankcase oil- once this small reserve of oil is exhauted, running in carries on with normal cylinder lube oil. The flow of oil is increased to carry away metallic particles.

Problems caused by stuffing box leakage oil entering crankcase

Low speed engines are particularly at risk from crankcase lubricant contamination caused by cylinder oil drainage past the piston rod gland and combustion products. This can lead to severe damage of engine crankcase components and reduction of life of oil which is normally expected to last the lifetime.

There has been a general increase in the viscosity and Base number of crankcase oils over recent years particularly for engines built since the early 1980’s. Increased alkalinity, viscosity and insolubles, fuel derived elements such as vanadium and oil additive derived elements such as calcium, suggest that the contamination is from the cylinder oil drainage.

Deterioration of the crankcase oil has led to the expensive necessity of replacing up to 50% of the sump, this is particularly of concern as it is often only a temporary measure.

Four causes are put forward,

  1. New crankcase oil contaminated with new cylinder oil-unlikely
  2. Cylinder oil drainings being recycled and returned to the sump-very likely as it is a common practice to purify oil leaking through the gland, tests done on this purified oil found high amounts of insolubles
  3. Leakage past rod gland- very likely, high pressure scavenge air can blow cylinder oil and dirt past the top scrapper ring and sealing rings into the piston rod drain tank, and even possibly directly into the sump. A problem that worsens with age and wear.
  4. leakage of exhaust valve lubrication system-unlikely

From above the suggestion is the most likely cause for contamination is leakage past the piston rod. It is seen that maintenance of the stuffing box is of the utmost importance. Tell tales and drainage lines should be proved free and use of oil drained from the uppermost drain should not be allowed even after purification due to the high level of contamination which can destroy the properties of the oil in the sump

I know of a case where due to the increased viscosity of the oil a 50% charge of hydraulic oil was added to the sump of a very large slow speed engine under advice from the manufacturer

Properties of Lubricating Oil

Composition of lubricating oils

Lubricating oil fractions extracted from crude oil are a widely varying mixture of straight and branched chain paraffinic, napthenic aromatic hydrocarbons having boiling points ranging from about 302o to 593oC. Some specialty lubricants may have boiling point extremes of 177 and 815oC. The choice of grade of lubricating oil base is determined by the expected use.

General capabilities expected from an engine lubricant

    • Dispersivity or capacity to the cold parts of an engine clean
    • Detergency or capacity to keep hot parts of an engine clean
    • Thermal strength or capacity to withstand temperature changes
    • Anti-oxidant or capacity to resist the action of oxygen
    • Anti-wear or capacity to contain wear
    • Anti-scuffing or capacity to preserve oil film even in the presence of high pressures
    • Alkalinity reserve or capacity to neutralise acids formed during combustion or other sources thereby preventing corrosive wear
    • Demulsibility or capacity to separate contaminants
    • Resistance to hydrolysis or capacity to withstand the action of water which can affect additives
    • Pumpability
    • Centrifugibility and filterability or capacity to separate insoluble elements
    • Anti-rust,corrosive and anti-foam are just some of the other properties required

Properties ideal for bearings

    • Soluble for high speed fluid film hydrodynamic lubrication, hence, low viscosity with reduced oil film friction.
    • moderate bearing loads
    • improved heat transfer behavior
    • corrosion protection
    • cooling
    • low friction
    • good low temperature viscosity
    • good high temperature viscosity

Properties ideal for gear case

    • high film strength to prevent metal to metal contact. Hence, high viscosity adhesive to resist sliding and centrifugal forces
    • corrosion protection
    • cooling
    • reduces friction
    • good low tempo viscosity
    • good high tempo viscosity The thicker the oil film the greater the cushioning against shocks. Also less tendency for pit formation by hydraulic action in cracks,
    • sound damping properties with cushioning effects
    • antifoam properties

Turbine oil
Compromise between above two requirements

    • Generally a good quality refined mineral oil derived from paraffanic base stock used with various additives including EP additives for highly loaded gearing.
    • Anti-foaming properties important

Additives

Improvements in lubricating oil over the last twenty years have come about almost entirely from the use of additives.

 

These are added for three main reasons;

  1. to protect the lubricant in service by limiting the chemical change and deterioration
  2. To protect the mechanism from harmful combustion products and malfunctioning lubricating oil
  3. To improve existing physical properties and to create new beneficial characteristics in the oil

Typical additives are; Barium, calcium, phosphorus, Sulphur, chlorine, zinc, oxidation inhibitor-increases oil and machinery life, decreases sludge and varnish on metal parts

Corrosion inhibitor– protects against chemical attack of alloy bearings and metal surfaces.

Antiwear improvers– protects rubbing surfaces operating with this film boundary lubrication. One such antiwear ( and oxidation inhibitor) chemical is Zinc dithiophosphate or ZDDP

Detergent– tend to neutralise the deposits before formation under high temperature and pressure conditions, or as a result of using a fuel with high sulphur content.

Dispersant– used to disperse or suspend the deposits forming contaminants. Typical dispersants, such as polyesters and benzlamides, are usually clean burning. The molecules have a polar charge at one end which attracts and holds the deposits

Alkaline agents– neutralises acids, htese form the TBN of the oil and includes additives such as the above dispersants and detergents. An excess of acid neutralising alkalis are present in the oil and these help to keep parts clean. Failure to keep an oil alkaline can lead to damage to bearings due to acidic attack as well as increased liner wear.

Rust inhibitors– protect to form the oxidation of metal component.

Pour point depressants– improves low temperature viscosity

Oiliness agent– reduces friction seizure point and wear rates

EP additives– increases film strength and load carrying capability

Antifoam agents– prevents stable bubble formation

Viscosity Improvers– an additive that improves the viscosity index of the oil. I.e. reduces the effect of temerpature of the oil.

Metal deactivators– prevent catalytic effects of metal

Antiseptic– bactericide.

Oxidation

Oxidation degrades the lube oil producing sludges, varnishes and resins. Presence of moisture, and some metals particularly copper tend to act as a catalyst. Once oxidation starts, deterioration of the properties of the oil is rapid.

Recharging

When recharging no more than 10 % of the working charge should be topped up due to heavy sludgeing that can occur due to the heavy precipitation of the sludge.

EP additive oils

Can assist in healing of damaged gear surfaces but should be used as a temporary measure only due to risk of side effects

Emulsification

This occurs due to water contamination; also, contamination with grease, fatty oils, varnish, paint and rust preventers containing fatty products can also promote emulsification.

The presence of an emulsion can be detected by a general cloudiness of the sample. Salt water emulsifies very easily and should be avoided.

Water entrained in the oil supplied to a journal bearing can lead to loss of oil wedge, rub and failure.

Fresh water contamination whilst not in itself dangerous can lead to rusting. The iron oxides catalyses the oil to form sludge’s. The additives in the oil can leach out to change the water into an electrolyte.

Salt water contamination is very serious as it causes tin oxide corrosion, and also leads to electrochemical attack on the tin matrix in the white metal. The sea water act as then electrolyte.

A major problem of water within a lub oil is where the mix enters a bearing, here it is possible for the water to be adiabatically heated causing it to flash off collapsing the oil wedge.

Stresses on Lube oil

The main stresses experienced by Lube oils in diesel engines operating on heavy fuel oils are expressed as follows

Acid Stress– Caused by sulphuric and oxidation acids. This leads to increased corrosive wear, deposits, reduced Base Number and shorter oil life.Rapid depletion of the BN is the clearest sign of oil stress

Thermal/Oxidative stress-This caused by elevated temperatures leading to increased rates of thermal/oxidative breakdown of lubricant and fuel. This leads to increased levels of deposits, sludges, corrosive wear of bearing material, oil thickening and reduced oil life. In addition deposits on the under crown side of the piston can lead to increased hot corosion on the piston.

Asphaltene Stress-This caused by fuel contamination of the lube oil and can lead to increased levels of deposits, sludges, lacquers, oil thickening and reduced oil life. In addition deposits on the under crown side of the piston can lead to increased hot corosion on the piston

OIL ANALYSIS

Regular testing of crankcase lub oil is important to ensure that deterioration has not taken place. The results of in service deterioration could be a reduction in engine protection or actual attack on working points by corrosive deposits. Oil samples are generally tested every 3 to 4 months depending on the system and experience. Shipboard testing is taking a rising prominence to allow monitoring of oil condition between testing.

To ensure good representation, care should be taken where the sample is drawn

Correct

    • Main supply line
    • inlet or outlet from l.o. cooler
    • Outlet from main l.o. pump

Incorrect

    • standpipes
    • purifier outlet
    • purifier direct sump suction

Samples should be drawn over a period of several minutes

Viscosity

The viscosity is the most important property of the oil. Oil of correct viscosity will provide optimum film strength with minimum friction losses and leakage.

The viscosity of a L.O. may fall due to fuel dilution if running on gas oil, and rise if running on heavy f.o. Viscosity may also increase due to heavy soot loading if purifiers and filters not operating efficiently. Oil ageing caused by oxidation and thermal degradation increases viscosity.

A simple shipboard test is the Mobil flow stick where drops of new and used oil are placed in separate channels on an inclined ‘stick’. The rate the oil flows down the stick is proportional to its viscosity.

Water content

Initially determined by ‘crackle’ test. The presence of Na and Mg in a 4:1 ratio indicates salt water contamination.

Limits are laid down by the manufacturer, but as a rule of thumb a limit of 0.2% should cause investigation into source and remedial action at 0.5%

Gross contamination can be remedied by placing the charge in a separate tank and heating to 70oC and circulating through purifier.

Spectrometry

Indicates the presence of metal element composition and identifies additive and contaminant levels.

Zinc(Zn),Phosphorus(P)– are components of many oils such as diesel engine oils, hydraulic oils and gear oils, to enhance antiwear and over properties of the oil

Calcium(Ca)- primarily a component of engine oils, provides detergency,alkalinity and resistance to oxidation. Residual fuel engine oils have higher Ca levels

Nickel(Ni)- Bearings, Valves, gear plating, fuel derivative

Barium(Ba)– Multi purpose additive, declining importance

Magnessium(Mg)– as for Ca, may also be due to sea water contamination if found in Ratio of 1:4 of Na

Chromium(Cr)– Piston rings, hydraulic actuator cylinders

Manganese(Mn)– Cylinder wear

Aluminium(Al)– generally comes from wearing piston skirts, levels rise where new piston fitted to old engine. Typically 10ppm, but rises during bedding in. May also indicate the presence of catylytic fines in residual fuels.

Iron(Fe), Molybdenum(Mo), Chromium(Cr)– metals alloyed for piston ring etc, a rise in level may indicate ring pack/liner wear.

Copper(Cu), Lead(Pb) , Tin(Sn), Silver(Ag) – soft metals used in the overlay of shell bearings, and phosphor bronze gears.Note that high copper content can also occur when samples are drawn from copper pipes which have not been flushed as well as gear wear.

Silicon(Si)– Indicates poor air filtration, possible fuel derivative

Sulphur(S)– May indicate the presence of clay based (bentonite) greases

Sodium(Na)– With Mg indicates the presence of sw contamination, possible coolant system and fuel derivative

Vanadium(V)- Usually indicates the presence of fuel oil

Alkalinity and acidity

TBN-TOTAL BASE NUMBER– measure of alkaline additives available for the neutralisation of acids from combustion products and oxidation. Level governed by type of fuel.

For crosshead engines the TBN will tend to rise due to contamination by liner lubrication, it should not be allowed to raise more than twice that of the new charge.

As a guide, the TBN of fresh oil should be at least:

    • 10 x fuel sulphur content (%) for trunk piston engines (10mgKOH/g)
    • 20 x fuel sulphur content (%) for cyl oil in x-head engines (20mgKOH/g)

A simple shipboard go,no-go test is available for measuring the TBN, it involves the addition of an indicator and acid reagent to a 30ml sample. The quantify of acid reagent added is determined by the required level of TBN, for TBN2.5 0.5ml are added, for TBN20 4ml is added. After three minutes the colour is checked against a chart

    • Purple:Good level of TBN
    • Green:Borderline
    • Yellow:Low level of TBN

TAN-TOTAL ACID NUMBER-measure of organic acid and strong acid content of oil. Where SAN is nil, the TAN represents the acidity in the oil due to both the acids in the additives and the oxidation of the hydrocarbons in the oil. The TAN of fresh oils varies with oil type, and tends to climb with age. A high TAN may indicate that an oil should be changed or freshened by top up. A high TAN may be accompanied with increased viscosity.

SAN-STRONG ACID NUMBER-indicates the prescience of strong, highly corrosive (inorganic) acids, usually formed from combustion products. If SAN is non zero the oil should be changed immediately

Oil cleanliness

IC-INDEX OF COMBUSTION-measures soot loading of oil

MD-MERIT OF DISPERSANCY-Ability of an oil to disperse contaminants, such as soot, wear debris and water and thereby carry them away from the critical areas. Measured by oil blot test and should not be allowed to fall below 50

DP-DEMERIT POINTS– combination of IC and MD: the lower the value, the healthier is the condition of the oil

Shipboard water content test

  1. The flask is filled to mark ‘A’ with kerosene
  2. A capsule of reagent (calcium hydride) is added. Any water in the kerosene will react with the calcium hydride and any gas vented off.

T

  • he container is topped to mark ‘B’ with sample oil
  1. The screw valve and cap are closed.
  2. The flask is inverted and shaken
  3. After 2 minutes the screw valve is opened. The hydrogen produced by the reaction between the reagent and water exerts a pressure which forces the kerosene through the open valve into the graduated cylinder. The amount discharged is proportional to the water content in the oil sample.
  • If the water content is greater than 1.5% then the test should be repeated this time using a smaller sample by filling only to mark ‘C’. The second scale on the graduated cylinder should then be used.
  • If water is detected its type, sea or fresh , should then be determined by use of a special reagent the water

PROPERTIES OF FUEL OIL

DENSITY:

Density is the absolute relationship between mass and volume at a stated temperature. The SI unit is kg/m 3 at a reference temperature, typically 15°C.

RELATIVE DENSITY:

Relative density (RD) of a substance is the ratio of the mass of a given volume at a temperature t1 to the mass of a given volume of pure water at temperature t2. Like specific gravity, RD is a ratio and hence no units. For example, RD at 20/4°C. Since 1m 3 of pure water at 4°C has a mass of 1000kg, the density of a substance at t1°C is equivalent to the RD at t1/4°C.

API:

In the United States and some other countries, the density of petroleum products is defined in terms of API gravity. This is an arbitrary scale adopted by the American Petroleum Institute for expressing the relative density of oils.

API= (141.5/RD at 60/60oF) – 131.5

Density in vacuum and in air

The terms ‘density in vacuo’ or ‘density in air’ are sometimes used on fuel delivery or bunker receipt notes. As density is the absolute relationship between mass and volume and not its weight to volume, by definition density is in vacuo. Although often used, the term ‘density in air’ is incorrect and should be referred to as a ‘weight factor’. This is because a substance weighed in air is supported to a small extent by the buoyancy of air acting on it. Thus the weight of a liquid in air is slightly less than the weight in vacuo. There is no simple relationship between density and ‘weight factor’ but for bunker fuels the difference approximates to 1.1 kg/m 3 . To convert density at 15°C to the ‘weight factor’ at 15°C, 1.1 kg/m3  should be deducted.

Density adjustment at temperatures other than 15oC:

Densities are measured over a range of temperatures, usually for convenience, at the temperature at which the fuel is stored. The value is then corrected back in test equipment or by the use of standard tables to the reference temperature.

DYNAMIC VISCOSITY

Dynamic viscosity also termed as absolute viscosity, is the tangential  force per unit area required to move one horizontal plane with respect to the other at unit velocity when maintained a unit distance apart by the fluid. When the fluid thickness is 1 cm, the force 1 dyne/cm2, the velocity 1cm/s the absolute viscosity is 1 POISE.

As the units are large it is more common to divide them by 100, resultant smaller units being CENTIPOISE.

1 centipoises= 1 millipascale second. [Pascal= 1N/m2]

The SI symbol is ‘ή’ and SI unit is N.s/m2.

CENTISTOKE

KINEMATIC VISCOCITY: It is the ratio of viscosity to the density of fuel.

Unit of kinematic viscosity is CENTISTOKE (cst) = centipoise / density

It can be found out that 1 cSt =10-6m2/sec.

VISCOSITY OF ORDERED FUEL

Fuel may have been ordered to one of the grades in ISO 8217, frequently on delivery, only the viscosity grade is stated. For example IF 180 this means that the viscosity is a maximum of 180 cSt at 50°C.

VISCOSITY TEMPERATURE RELATIONSHIP

Because of the viscosity/temperature relationship, a few degrees change could make a big difference to the injection viscosity. In practical terms, this means that if the actual fuel viscosity is greater than that ordered, it is likely that the fuel oil heater can accommodate this.

VISCOSITY TEMPERATURE RELATIONSHIP

Required viscosity for combustion in Engine

Required viscosity for combustion of Heavy oil is about 13 to 17 cSt.

The viscosity of Diesel oil is about 7 cSt or less.

INJECTION TEMPERATURE FOR VARIOUS GRADES OF VISCOSITY.

VISCOSITY INDEX:

It is a numerical value which measures the ability of the oil to resist viscosity change when the temperature changes.

A high viscosity index would refer to an oil capable of maintaining a fairly constant velocity value in spite of wide variation in the temperature.

The value of viscosity index is usually determined from a chart based on knowledge of the viscosity values at different temperatures.

CCAI  & CII

CCAI and CII are empirical attempts to estimate how long the fuel will take from injection to ignition and they are also an implication of the likelihood of engine damage.

EFFECT OF TIME BETWEEN INJECTION AND START OF INJECTION.

Fuel takes a finite time from the start of the injection to the start of combustion.

During this period, fuel is intimately mixed with the hot compressed air in the cylinder where it begins to vaporize.

After a short delay known as the ignition delay, the heat of compression causes spontaneous ignition to occur.

Rapid uncontrolled combustion follows as the accumulated vapour formed during the initial injection phase is vigorously burned.

The longer the ignition delay, the more fuel will have been injected and vaporized during this “pre-mixed” phase and the more explosive will be  the initial combustion.

EFFECT OF TIME BETWEEN INJECTION AND START OF INJECTION.

Rapid pre-mixed combustion causes very rapid rates of pressure rise in the cylinder resulting in shock waves, broken piston rings and overheating of metal surfaces.

Large diesel engines are designed to withstand a certain rate of pressure rise within the cylinder although the figure will vary between different designs.

Rate of pressure rise due to ignition delay.

The ignition quality of a fuel is a measure of the relative ease by which it will ignite. For distillate fuels, this is measured by the cetane number. Cetane number is determined by testing in a special engine with a variable compression ratio. The higher the number, the more easily will the fuel ignite in the engine.
For residual fuel, there are two accepted empirical equations both based on the density and viscosity of the fuel. These are the Calculated Carbon Aromaticity Index (CCAI) and Calculated Ignition Index (CII). The CCAI gives numbers in the range 800-870, while the CII gives values in the same order as the cetane index for distillate fuels. Of the two equations, CCAI values are more frequently quoted.

The figure is a nomogram which incorporates both CII and CCAI. If the viscosity is fixed and the density is raised, the CII value falls and the CCAI value is increased. Similarly, if the density is fixed and the viscosity lowered, the CII value falls and the CCAI value is increased. In general, values less than 30 for CII and greater than 870 for CCAI are considered problematical. If required, further guidance on acceptable ignition quality values should be obtained from the engine manufacturer.

CCAI

CCAI = d – 81- 141 log log(VK + 0.85)

d = density kg/m^3

VK = viscosity in mm^2/s at 50oC

CETANE NUMBER

It is an indication of the ignition quality of the fuel.

In a compression ignition engine the time interval between fuel injection and firing, called ignition delay, must not be too long otherwise collected fuel will generate high pressures when it ignites and diesel knock results.

Paraffin hydrocarbons have the best ignition quality.

Cetane number and density

Density is often indicative of cetane number especially in the middle ranges, i.e., density 850 kg/m3, cetane number about 61, density 950 kg/cm3, cetane number about 37.

Acetone peroxide used as additives to improve cetane number.

Calorific Value

The specific energy of a fuel expressed in MJ/kg depends on the composition. For residual fuel, the main constituents are carbon and hydrogen, both of which release energy on combustion. Sulphur also releases energy on combustion but to a lesser extent than carbon and hydrogen.

CARBON RESIDUE:

The carbon residue of a fuel is the tendency to form carbon deposits under high temperature conditions in an inert atmosphere. It may be expressed as Ramsbottom Carbon Residue (RCR), Conradson Carbon Residue (CCR) or Micro Carbon Residue (MCR). Numerically, the CCR value is the same as that of MCR. The carbon residue value is considered by some to give an approximate indication of the combustibility and deposit forming tendencies of the fuel.

CARBON RESIDUE:

The carbon residue value of a fuel depends upon the refinery processes employed in its manufacture. On a global basis, this is typically 15-16% m/m but in some areas can be as high as 20% m/m.

  • CCAI:
  • The ignition quality of a fuel is a measure of the relative ease by which it will ignite
  • There is accepted empirical equations based on the density and viscosity of the fuel. These are the Calculated Carbon Aromaticity Index (CCAI) range 800-870
  • CCAI- Effect on engine type 4 stroke engines
  • Ignition quality- engine damage
  • FIA-Fuel ignition analyser
  • Ignition delay & Rate of heat release ROHR- New technology
  • Flash point
  • The flash point of a fuel is the temperature at which vapour given off will ignite when an external flame is applied under specified test conditions. A flash point is defined to minimise fire risk during normal storage and handling.
  • The minimum flash point for fuel in the machinery space of a merchant ship is governed by international legislation and the value is 60o For fuels used for emergency purposes, external to the machinery space, for example the lifeboats, the flash point must be greater than 43oC.
  • Residual fuels are capable of producing light hydrocarbons in the tank headspace, near to or within the flammable range. Hence all residual fuel oil headspaces should be considered to be potentially flammable.
  • Sulphur
  • residual fuel the value is in the order or 1.5-4 % m/m.
  • marginal effect on the specific energy
  • The corrosive effect of sulphuric acid during combustion is counteracted by adequate lube oils and temperature control of the combustion chamber
  • Carbon residue
  • The carbon residue is measured as Conradson Carbon or as Micro carbon.
  • cause increased fouling of the gasways, necessitating more frequent cleaning, especially of the turbocharger and exhaust gas boiler.
  • Fuels with a high carbon residue value may cause problems in older engines under part load conditions.
  • Water
  • The ingress of water can come from a number of sources, which include tank condensation and tank leakage
  • removed by centrifuging the fuel before use. This applies especially to salt water, the sodium content of which can result in deposits on valves and turbochargers.
  • If water cannot be removed, homogenizing after centrifuging is recommended.
  • Ash
  • Ash represents solid contaminants as well as metals present in the fuel in soluble compounds (vanadium). Part of the ash could be catalyst particles from the refining process.
  • Such particles are highly abrasive.
  • Solid ash should be removed to the widest possible extent by centrifuging, and cleaning can be improved by installing a fine filter after the centrifuge e.g 5 – 10 microns.
  • Vanadium and Sodium
  • Vanadium is present in the fuel in soluble compounds and, consequently, cannot be removed.
  • Vanadium, in combination with sodium, may lead to exhaust valve corrosion and turbocharger deposits.
  • This can occur especially if the weight ratio of sodium to vanadium exceeds 1:3, and especially in the case of a high vanadium content.
  • Vanadium deposits can be so hard that they can cause extensive damage to the TC nozzle ring and turbine wheel.
  • The only way to remove vanadium depositsis to disassemble the components and remove the deposits mechanically.
  • Vanadium & Sodium- High temperature corrosion
  • Vanadium and Sodium
  • Sodium is normally present in the fuel as a salt water contamination and may, as such, be removed by centrifuging.
  • Sodium can also reach the engine in the form of airborne sea water mist.
  • Aluminium and silicon
  • Aluminium and silicon limits content of catalytic fines, mainly Al2O3 and SiO2, in the oil. 80 mg Al and Si corresponds to up to 170 mg Al2O2 and SiO2.
  • Catalytic fines give rise to abrasive wear, reduced by centrifuging the fuel oil before it reaches the engine, and 5- 10 micron fine filter after the centrifuge
  • Catalytic fines imbedded in piston ring

Don’t get me wrong; I am not suggesting that commercial oil analysis labs are duping their clients by shortchanging testing services. Many of these missing tests cannot be practically performed on routine oil samples because they are expensive, involve prolonged test periods and/or require large sample volumes. Yet it is important that the user community fully understand what they get and what they don’t get when they pay $35 for oil analysis.

Performance Tests 
Below is a list of “performance” tests that are often used to portray the quality and performance capabilities of a new lubricant. Unlike ordinary used oil analysis tests that report physical and chemical properties such as viscosity, acid number, flash point, elemental analysis and contamination, performance tests work by challenging a lubricant in some way similar to the actual machine work environment. The reported results characterize or measure how the lubricant responded to the challenge. The following are typical examples of performance tests:

Film Strength. There are numerous ASTM test methods that attempt to depict or measure a lubricant’s ability to reduce friction and control wear under wide-ranging rolling and sliding conditions. Adhesive wear, contact fatigue and two-body abrasion are examples of wear modes affected by a lubricant’s film strength. Antiwear and extreme pressure (EP) additives are added to many lubricant formulations for this purpose. These additives are subject to depletion and impaired performance as a lubricant ages and becomes contaminated. Conventional used oil analysis tests do not measure film strength.

Air-handling Ability. The quality of a lubricant’s basestock and the use of certain additives can define its air-handling abilities. We want a lubricant to release entrained air rapidly and to suppress the formation of foam. Air handling is nearly impossible to interpret from ordinary oil analysis.

Water-handling Ability. Like air handling, the lubricant’s ability to efficiently shed water during static conditions is difficult to anticipate from the usual slate of oil analysis tests. Yet for most lubricants, a loss of water-handling ability not only reveals risks from oil-water emulsions but also signals faltered performance of other important properties. This property too often goes unnoticed by the used oil analysis community.

Corrosion Control. Corrosion control is a fundamental lubricant formulation objective. There are many additives used to neutralize corrosive agents or form protective barriers on sensitive machine surfaces. These are sacrificial additives that lose their effectiveness over time. Nonetheless, no conventional used oil analysis test, other than the base number, reports the residual effectiveness of the corrosion-protecting qualities of an in-service lubricant.

Oxidation Stability. With rare exception, nearly all lubricants are formulated with oxidation inhibitors to stem the rate of oxidation. The most robust and superior lubricants on the market today emphasize this important lubricant property. These include premium turbine oils, long-mileage motor oils and synthetic lubricants of all types. While post-oxidation by-products can be detected and measured by ordinary oil analysis tests (after the fact), the residual oxidation stability of a lubricant is far more difficult to assess. That said, some success has been reported with techniques such as linear-sweep voltametry and infrared spectroscopy (additive spectral bands). These tests are becoming increasingly common in commercial oil analysis, although used on less than five percent of all samples tested.

Besides those properties listed above, there are numerous other performance properties that are application- and lubricant-type specific. These include volatility, resistivity, biodegradability and thermal stability. And there is a slew of properties relating specifically to grease formulation including consistency, dropping point, separability, water wash-out, pumpability, etc.

“Boiler Survey”

BOILER SURVEY

 

 

Introduction

 

         Boilers are inspected to maintain the regulatory requirement. Regular internal and external examination during such survey constitutes the preventive maintenance schedule the boiler goes through to have a safe working condition.

 

Interval:

           

          Boilers require to be surveyed at 2-year intervals until they are 8 years old, thereafter they become due for survey annually.

 

Procedures

 Planning

  1. Discuss with Master and Chief Engineer to confirm time available, manpower and time required and steam requirement for next port.
    1. Checks before shutting down boiler:
    2. Sufficient spares (joints, packing, gauge glass, etc)
    3. Past reports and manual for special attention need to be take care
  2. Special Tools required
  3. Meeting and brief with all engineers involved
  4. Mark all valves, safety valve setting and spigot clearance

 

Before shutting down boiler

  1. Inform Chief engineer
  2. Inform duty deck officer
  3. Top up DO service tank
  4. Change over M/E, A/E and boiler to Diesel oil
  5. Stop all purifier
  6. Shut all heating and tracing steam valve
  7. Soot blow the boiler

 

 

Shutting down Boiler

  1. Change over to manual firing
  2. Stop firing
  3. Purge boiler for 5 minutes
  4. Shut main steam stop valve
  5. Switch off power, off the circuit breaker and remove fuses for FD fan, FO pumps, feed pumps and control panel.
  6. Put a notice on the circuit breaker mentioned above
  7. Shut all fuel valve and atomizing valve and lock them in shut position, blank the line if necessary
  8. Allow boiler to cool down slowly
  9. Scum blowdown follow by bottom blowdown when the boiler cooled
  • Open air vent when boiler pressure drop until 2 bar to prevent vacuum formation
  • Further cooling of boiler
  • Prepare to open top manhole door when boiler is cooled and at atmospheric pressure
  • Slacken the dog nut and secure manhole with rope
  • Knock manhole door gently with long stick. Do not open fully because hot steam or water might gush out.
  • Open full when is safe
  • Allow further cooling of boiler before open the bottom manhole door. This is to prevent thermal shock
  • Confirm no large quantities of hot water lying in the bottom
  • Open the bottom manhole door with the same precaution as with the top manhole door
  • Open the furnace door slowly
  • Ventilate the boiler both water and fire side for 12-24 hours
  • Enclose space entry permit obtained
  • Check Oxygen, flammable gas and toxic gas content
  • Prepare to entry

 

Preparation for entry

  1. Prepare safety torch and safety hand lamp
  2. Investigate from outside make sure it is clear from obstruction before entering boiler
  3. Oxygen analyzer is carry with the person entered boiler
  4. Personnel entering must wear all safety gears
  5. Clear pocket contents and tools to be carried in a bag and accounted
  6. A responsible engineer to be standby outside with clear emergency order
  7. Keep breathing apparatus ready
  8. Remain communication
  9. Ensure proper lighting at all time

 

Boiler Inspection

  1. Thoroughly cleaned before boiler is surveyed
  2. Wire brush and hose down may be sufficient to prepare for survey in well maintained boiler
  3. Chipping off scale is necessary
  4. If traces of oil are found in boiler, chemical means may have to be adopted to remove them

 

Route of inspection

  1. Gas Side

    1. Exterior of drums for signs of tube roll, leakage, corrosion, soot erosion and overheating
    2. Condition of outside drum insulation
    3. Drum seals for sign of air leakage
    4. Inspect drum support for crack and expansion clearance
    5. All blowdown connections for expansion and flexibility of support
    6. All piping and valve for leaks
    7. Water wall tubes and fins for crack
    8. Exterior of all tubes for corrosion, carbon build up, erosion, blisters and sagging
    9. Tubes near soot blowers for steam impingement
    10. Condition of refractory
    11. Around burner assembly, refractory and accumulation of soot or carbon
    12. Soot blower for distortion, worn bearings, rubbing of tubes, condition of nozzles, cracks, freedom of movement and effective lubrication

 

  1. Water side

    1. Steam drum for corrosion scaling and pitting
    2. Manhole seats and surface
    3. Condition of all fee, chemical feed, blowdown lines and inside pressure parts for choking, security and leaks
    4. Tubes for corrosion, excessive deposits, flare cracking and pitting
    5. Hand hole plates and stud threads

 

  1. Safety Valve

    1. Condition of valve internal parts for signs of corrosion, galling and wear
    2. Check for pitting, crack, resiliency and condition of springs
    3. Check spindle for straightness and adjusting ring thread for freedom of movement
    4. Check discharge and drain piping

 

  1. Check dampers to ensure that linkage are secured and well greased
  2. Condition of burners, swirler and air register
  3. Wind-box dampers and vanes for sign of corrosion and erosion
  4. Check condition and operation of all valve
  5. Check feed water controller and control valve connection lines and ensure proper functioning
  6. Examine the foundation and bracing bolts of boiler for corrosion, fretting and rusting

 

 

Closing

  1. Inspect internal surface to ensure they are clean
  2. Counter check all tools are out from boiler
  3. All opening of the mounting are cleaned properly
  4. Mountings to be fixed back with new set of gasket/joint
  5. Replace the header handhole and the bottom manhole door
  6. Operate all mounting valves to ensure they work freely and leave all valves in close position

 

  1. Replace top manhole door
  2. Sootblower are correctly fitted
  3. Air control dampers move freely for their full travel
  • Open gauge glass steam and water cocks and shut drain cock
  • Open vent, alarm and pressure gauge connection valve
  • Shut all drain valve
  • Switch on power for control panel, feed pump, FD fan and FO pump
  • Fill boiler with hot distilled treated water
  • Fill until water level below normal level
  • Check control air is available

 

Flashing Up

  1. Start FD fan and purge boiler for 5 minutes
  2. Start FO pump and check all parameters
  3. Fire boiler with minimum firing ratio
  4. Continue firing intermittently e.g. 1min. fire, stop 10min. for 1st hour, 2min fire, stop 10min. for 2nd hour and so on….
  5. As boiler heats up, water level will rise to normal level, top up if necessary
  6. Continue fire until a continuous stream of steam comes out from air vent
  7. Shut air vent
  8. Blow through gauge glass when boiler pressure raised
  9. Open valve to remote level indicator
  • At 7 bar, all securing buts to be retighten
  • Open steam line drains to drain off condensate
  1. Warm up the steam line
  2. Gag 1 safety valve, raise the steam pressure slowly and check valve lift pressure and adjust accordingly
  3. Repeat the procedure for other safety valve
  4. Ensure no condensate at the drain line
  5. Crack open main steam stop valve, slowly open until its full open
  6. Keep firing as steady as possible
  7. Check all safety cut outs and alarms before putting boiler on Auto
  8. Final round check on boiler
  9. Start tanks and tracing steam heating
  10. Open steam to all heaters
  11. Start all purifier
  12. Change over from DO to HO for boiler and Generator

 

  • M/E change over during departure

 

EGE Safety valve

  1. C/E to set the safety valve when the ship is at sea
  2. Report to surveyor in writing to confirm safety valve operation

“A Short Note on MARPOL Regulations”

MARPOL

 What is MARPOL?

– International Convention for the Prevention of Pollution from Ships,

1973, as modified by the Protocol of 1978.

 Introduction

The MARPOL Convention is the main international convention covering prevention of pollution of the marine environment by ships from operational or accidental causes. It is a combination of two treaties adopted in 1973 and 1978 respectively and updated by amendments through the years.

The International Convention for the Prevention of Pollution from Ships (MARPOL) was adopted on 2 November 1973 at IMO and covered pollution by oil, chemicals, harmful substances in packaged form, sewage and garbage. The Protocol of 1978 relating to the 1973 International Convention for the Prevention of Pollution from Ships (1978 MARPOL Protocol) was adopted at a Conference on Tanker Safety and Pollution Prevention in February 1978 held in response to a spate of tanker accidents in 1976-1977. (Measures relating to tanker design and operation were also incorporated into a Protocol of 1978 relating to the 1974 Convention on the Safety of Life at Sea, 1974).

As the 1973 MARPOL Convention had not yet entered into force, the 1978 MARPOL Protocol absorbed the parent Convention. The combined instrument is referred to as the International Convention for the Prevention of Marine Pollution from Ships, 1973, as modified by the Protocol of 1978 relating thereto (MARPOL 73/78), and it entered into force on 2 October 1983 (Annexes I and II).

 

Objectives

To eliminate the pollution of the sea’s by oil, chemicals and other harmful substances which might be discharged during the operation To minimize the amount of oil that which is released due to accidents, collisions, groundings etc.

 

MARPOL ANNEXES:

 

At present, there are 6 annexes in MARPOL:

Annex I: Prevention of pollution by oil
Annex II: Control of pollution by noxious liquid substances
Annex III: Prevention of pollution by harmful substances in packaged form
Annex IV: Prevention of pollution by sewage from ships
Annex V: Prevention of pollution by garbage from ships                                                                                                      Annex VI: Prevention of  Air Pollution from Ships

 

 

Special Area:

Means a sea area where for recognized technical reasons in relation to it’s oceanographically and ecological condition and to the particular character of its traffic the adoption of special mandatory methods for the prevention of sea pollution is required.

 

In Annex I Prevention of pollution by oil, Annex II Control of pollution by noxious liquid substances, Annex IV Prevention of pollution by sewage from ships and Annex V Prevention of pollution by garbage from ships, MARPOL defines certain sea areas as “special areas” in which, for technical reasons relating to their oceanographical and ecological condition and to their sea traffic, the adoption of special mandatory methods for the prevention of sea pollution is required. Under the Convention, these special areas are provided with a higher level of protection than other areas of the sea.

Annex VI Regulations for the Prevention of Air Pollution from Ships establishes certain sulphur oxide (SOx) Emission Control Areas with more stringent controls on sulphur emissions.

Special areas under MARPOL are as follows:

Adoption, entry into force & date of taking effect of Special Areas

Special Areas

Adopted #

Date of Entry into Force

In Effect From

Annex I: Oil

Mediterranean Sea

2 Nov 1973

2 Oct 1983

2 Oct 1983

Baltic Sea

2 Nov 1973

2 Oct 1983

2 Oct 1983

Black Sea

2 Nov 1973

2 Oct 1983

2 Oct 1983

Red Sea

2 Nov 1973

2 Oct 1983

*

“Gulfs” area

2 Nov 1973

2 Oct 1983

1 Aug 2008

Gulf of Aden

1 Dec 1987

1 Apr 1989

*

Antarctic area

16 Nov 1990

17 Mar 1992

17 Mar 1992

North West European Waters

25 Sept 1997

1 Feb 1999

1 Aug 1999

Oman area of the Arabian Sea

15 Oct 2004

1 Jan 2007

*

Southern South African waters

13 Oct 2006

1 Mar 2008

1 Aug 2008

Annex II: Noxious Liquid Substances

Antarctic area

30 Oct 1992

1 Jul 1994

1 Jul 1994

​Annex IV: Sewage ​ ​ ​

​Baltic Sea

​15 Jul 2011

1 Jan 2013

​**

Annex V: Garbage

Mediterranean Sea

2 Nov 1973

31 Dec 1988

1 May 2009

Baltic Sea

2 Nov 1973

31 Dec 1988

1 Oct 1989

Black Sea

2 Nov 1973

31 Dec 1988

*

Red Sea

2 Nov 1973

31 Dec 1988

*

“Gulfs” area

2 Nov 1973

31 Dec 1988

1 Aug 2008

North Sea

17 Oct 1989

18 Feb 1991

18 Feb 1991

Antarctic area (south of latitude 60 degrees south)

16 Nov 1990

17 Mar 1992

17 Mar 1992

Wider Caribbean region including the Gulf of Mexico and the Caribbean Sea

4 Jul 1991

4 Apr 1993

1 May 2011

Annex VI: Prevention of air pollution by ships (Emission Control Areas)

Baltic Sea (SOx)

26 Sept 1997

19 May 2005

19 May 2006

North Sea (SOx)

22 Jul 2005

22 Nov 2006

22 Nov 2007

​North American 
(SOx, and NOx and PM)

​26 Mar 2010

​1 Aug 2011

​1 Aug 2012

​United States 
Caribbean Sea ECA 
(SOx, NOx and PM)

​26 Jul 2011

​1 Jan 2013

​1 Jan 2014

 

 

# Status of multilateral conventions and instruments in respect of which the International Maritime Organization or its Secretary-General perform depositary or other functions as at 31 December 2002.

 

* The Special Area requirements for these areas have not yet taken effect because of lack of notifications from MARPOL Parties whose coastlines border the relevant special areas on the existence of adequate reception facilities (regulations 38.6 of MARPOL Annex I and 5(4) of MARPOL Annex V).

 

** The new special area requirements, which will enter into force on 1 January 2013, will only take effect upon receipt of sufficient notifications on the existence of adequate reception facilities from Parties to MARPOL Annex IV whose coastlines border the relevant special area (regulation 13.2 of the revised MARPOL Annex IV, which was adopted by resolution MEPC.200(62) and which will enter into force on 1 January 2013).

 

Annex I: Prevention of pollution by oil

 

 

 

  • Regulation 14: Oil Filtering Equipment

Vessels above 400 GT and less than 1000 GT shall have an oil filtering equipment

  • Approved by the Administration
  • Will ensure that any oily mixture discharged into the sea after passing through the equipment has an oil content not exceeding 15 ppm

 

Vessels above 1000 GT shall have an oil filtering equipment

  • In addition to the above, shall be provided with alarm arrangements to indicate when the level cannot be maintained.
  • Also arrangements to ensure that any discharge of oily mixture is automatically stopped when the oil content of the effluent exceeds 15 ppm

 

Discharge from Machinery spaces:

 

  1. In special Areas : (Regulation 15)
  • The ship proceeding is en route
  • The oily mixture is processed through an oil filtering system
  • The oil content of the effluent without dilution does not exceed 15ppm.
  • When the vessel is in the special area the oil filtering system apart from having an alarm when the 15ppm cannot be maintained shall also be of a design where the oil filtering system shall stop automatically when the oil effluent exceeds 15ppm
  • Oily mixtures do not originate from the cargo pump room bilges in case of oil tankers
  • Oily mixtures in case of oil tankers is not mixed with oil cargo residues

 

  1. Outside special Area’s: (Regulation 15)
  • The ship proceeding is en route
  • The oily mixture is processed through an oil filtering system
  • The oil content of the effluent without dilution does not exceed 15ppm.
  • Oily mixtures do not originate from the cargo pump room bilges in case of oil tankers
  • Oily mixtures in case of oil tankers is not mixed with oil cargo residues

 

 

Exceptions

  1. he discharge into the sea of oil or oily mixture necessary for the purpose of securing the safety of a ship or saving life at sea; or
  2. the discharge into the sea of oil or oily mixture resulting from damage to a ship or its equipment:
  3. provided that all reasonable precautions have been taken after the occurrence of the damage or discovery of the discharge for the purpose of preventing or minimizing the discharge; and
  4. except if the owner or the master acted either with intent to cause damage, or recklessly and with knowledge that damage would probably result; or
  5. the discharge into the sea of substances containing oil, approved by the Administration, when being used for the purpose of combating specific pollution incidents in order to minimize the damage from pollution. Any such discharge shall be subject to the approval of any Government in whose jurisdiction it is contemplated the discharge will occur.

 

Regulation 17 Oil Record Book (PART 1)

  • Ballasting or Cleaning of fuel oil tanks
  • Discharge of dirty ballast or cleaning water from fuel oil tanks
  • Collection , Transfer and disposal of oil residues
  • Non automatic starting of discharge overboard, transfer or disposal otherwise of bilge water accumulated in machinery spaces
  • Automatic starting of discharge overboard, transfer or disposal otherwise of bilge water accumulated in machinery spaces
  • Condition of the oil filtering equipment
  • Accidental or other exceptional discharges of oil
  • Bunkering of fuel or bulk lubricating oil
  • Additional operational procedures and general remarks

 

FOR AN OIL TANKER DISCHARGING OIL FROM CARGO RESIDUES:

 

Regulation 29: Slop Tanks

Oil tankers above 150 GT shall be provided with a slop tank arrangement having the following provisions

  1. Adequate means provided for cleaning of cargo tanks and transfer of dirty ballast residues and tank washing from cargo tanks to slop tanks
  2. Slop tank arrangement should be such to allow the transfer or discharge of oily mixture in compliance with the discharge regulations
  3. The slop tanks to have a capacity of min 3% of the total cargo carrying capacity of the vessel. Maybe reduced to 2 or 1.5% if such an amount is sufficient for carrying out tank cleaning operations without the introduction of additional water into the system

 

Regulation 31: ODMCS/ ODME

Tankers above 150 GT shall be fitted with an ODMCS/ODME

  1. Must have a recording device to provide continuous record of the operation showing the ltrs/nm, total qty of oil disch ,the oil content and the rate of discharge
  2. Must be identifiable with date and time
  3. Should come into operation when there is any discharge of effluents to the sea and should be capable of stopping the operation if the instantaneous rate of discharge exceeds 30 ltrs/nm
  4. Failure to the system shall stop the operation
  5. In case of failure, the system may be used on manual mode but the defect to be repaired as soon as possible. Vessel maybe allowed to undertake one ballast passage with the defective equipment

 

 

 

 Regulation 34  Control of Discharge of oil For an OIL TANKER

 

  1. Outiside special areas
  2. Vessel should not be in a special area
  3. Vessel should be en route
  4. Vessel should be atleast 50 miles from the nearest land
  5. Any instantaneous discharge should not exceed more than 30 ltrs/nautical mile
  6. Total oil residue discharge less than 1/15000 of the product carried for tankers built before 31 Dec 1979
  7. Total oil residue discharged less than 1/30000 of the product carried for tankers built after 31 Dec 1979
  8. The tanker has in operation an ODMCS/ODME (oil discharge monitoring and control system) and a slop tank arrangement

 

 

  1. In Special Area(Regulation 34)
  • Any discharge into the sea of oil or oily residues from cargo spaces of an oil tanker is prohibited when in special area

 

REGULATION 36 ORB (PART 2) Cargo Oil record Book

 

Part2  is carried by the tankers and is for the cargo/ballast operations

Entries:

  1. Loading of oil cargo
  2. Internal transfer of oil cargo while on voyage
  3. Discharging of oil cargo
  4. Ballasting of the cargo tanks and Ballasting of the dedicated clean ballast tanks
  5. Cleaning of cargo tanks including crude oil washing
  6. Discharge of ballast except from the segregated ballast tanks
  7. Discharge of water from the slop tanks
  8. Closing of all applicable valves after slop tanks have been discharged
  9. Closing of valves for isolation of dedicated clean ballast tanks from cargo and stripping lines after slop tank discharge operations
  10. Disposal of residues
  11. Accidental discharge of any oil content and the reasons for the same
  12. Conditions of the oil discharge monitoring system and the failures of the same to be recorded too
  13. All the entries made need to be signed by the responsible officer along with the date and to be counter signed by the master. This record book needs to be maintained onboard for 3 years.

 

 

Regulation 37: SOPEP (Shipboard Oil Pollution Emergency Plan)

  1. Every oil tanker more than 150 gt and ship other than a tanker more than 400 gt shall carry and MUST have a SOPEP (shipboard oil pollution emergency plan)
  2. Procedures to be followed by the master or other persons having the charge of the ship to report an oil pollution incident
  3. List of authorities or persons to be contacted in event of any oil spill/pollution incident
  4. Detailed description of the actions to be taken to reduce or control the discharge of oil following the incident
  5. Procedures and point of contact on the ship for co-ordinating the shipboard actions with the national and local authorities in combating the pollution
  6. All oil tankers of 5000 tones deadweight or more shall have access to computerized shore based damage stability and residual structural strength calculation programs

 

 

Pollution prevention methods itemised on the tankers ship shore safety checklist

  • vessel should be securely moored
  • effective ship shore communication system established
  • emergency signals to be used by the ship and shore to be decided and understood
  • cargo hoses are properly rigged and not damaged
  • SOPEP equipments standby
  • Scupper plugs in place
  • High level alarms of the tanks to be operational

Checklist will also contain

  • Fire fighting equipments to be kept standby
  • Effective deck watch to be maintained to check any overflow
  • No unauthorised persons onboard
  • No unauthorised work to be carried out
  • No naked lights and flames
  • Tanks inerted and the inert gas systems checked
  • All doors to accommodation to be closed and the air conditioning systems to be on internal circulation
  • Appropriate lights and flags shown

 

Certificates issued under annex 1

International Oil Pollution Prevention (IOPP) Certificate

Surveys: Initial, Annual, Annual /Intermediate, Intermediate/Annual, Annual & Renewal

 

Attachments:

  • Form A: Listing equipments, arrangement & procedures in machinery spaces
  • Form B: Listing equipments, arrangement & procedures in cargo spaces

 

 

 Annex II: Control of pollution by noxious liquid substances

 

  • Entry into force: 6 April 1987
    (Revised Annex II enters into force 1 January 2007).
  • Annex II details the discharge criteria and measures for the control of pollution by noxious liquid substances carried in bulk.
  • Annex II: Substances indicated in chapter 17 or 18 of the International Bulk Chemical code

 

Regulation 6: Categories of substances

 

Category X: Noxious Liquid Substance (NLS) which if discharged into the sea from tank cleaning or deballasting operations are deemed to present a major hazard to either the marine environment or human health and therefore justify the prohibition of discharge into the marine environment

 

Category Y: Noxious Liquid Substance (NLS) which if discharged into the sea from tank cleaning or deballasting operations are deemed to present a hazard to the marine environment or to human health or cause harm to the uses of the sea therefore limitations are applied on the quantity and quality of discharge into the marine environment

 

Category Z: Noxious Liquid Substance (NLS) which if discharged into the sea from tank cleaning or deballasting operations are deemed to present a minor hazard to the marine environment or human health or marine resources and therefore less stringent restrictions apply  on the quality and quantity of discharge into the marine environment

 

Other Substances: Noxious Liquid Substance (NLS) other than X, Y & Z which at the moment do not pose any threat to the marine environment or human health on discharge into the sea from tank cleaning or deballasting operations.

 

Regulation 13: Discharge standards for Annex 2 (NLS) within and outside the Special area (applies to category X, Y & Z)

 

The discharge of these substances into sea is permitted with following discharge standards:

  • The ship is en route and doing a speed of atleast 7 knots in case of a self propelled ship or atleast 4knots in case of a non self propelled ship
  • The discharge is made below the water line through the underwater discharge outlets and not exceeding the rate by which the underwater discharge outlets are designed
  • The discharge is made at a distance of not less than 12 nautical miles from the nearest land and in the depth of water of not less than 25 metres.

 

Discharge Criteria for category X

  • Tank from which category X substance has been unloaded shall be subjected to a pre wash before the vsl leaves the port of unloading. The residues shall be discharged to port reception facilities until the concentration falls to 0.1% by weight by analysis. All remaining tank washings to be transferred until tank is empty. Entries to be made in the cargo record book
  • Any water subsequently added maybe discharged into the sea
  • Where it is not possible to find the concentration of the effluent without delaying the ship then alternate procedures maybe adopted to find the concentration provided that
  1. Tank is pre washed in accordance with the procedure adopted by the administration
  2. Appropriate entries are made into the cargo record book

 

 

Discharge Criteria for category Y & Z

  • If the unloading of the substance is not carried out in accordance with the manual, a pre wash to be carried out prior the vessel leaves the port of unloading. The tank washings to be discharged to shore reception facilities.
  • For high viscosity or solidifying substances in cat Y
  1. Pre wash to be carried out
  2. The residue to be discharged to shore reception facilities until tank is empty
  3. Any subsequent water introduced into the tank maybe discharged at sea

 

Regulation 14: P & A manual

 

  • Every ship certified to carry CAT X , Y & Z shall have an approved P&A manual.
  • The main purpose being to help identify the the physical arrangements and all the operational procedures w.r.t
  1. cargo handling
  2. tank cleaning
  3. slops handling
  4. cargo tank ballasting and deballasting.

 

Regulation 17: Shipboard Marine Pollution Emergency Plan (SMPEP)

 

Every ship above 150 GT certified to carry Noxious Liquid Substance (NLS) to have an approved SMPEP

  • Procedures to be followed to report a NLS pollution incident
  • List of authorities and persons to be contacted
  • Detailed description of actions to be taken to reduce or control the discharge of NLS
  • Procedures and point of contact on the ship for co-ordinating shipboard action with national and local authorities

 

Contents of a SMPEP

 

  • Reporting Requirements
  • Steps To Control Discharge
  • National And Local Co-Ordination
  • Additional Information
  • List Of Coastal State Contacts
  • List Of Ship Interest Contacts
  • Flow Chart And Checklists
  • IΜΟ Resolution A.851(20) & Resolution MEPC.138(53)
  • Vessel Specific Information

 

Entries in the Cargo Record Book

  • Loading of cargo
  • Internal transfer of cargo
  • Unloading of cargo
  • Mandatory pre wash in accordance with the ships P & A manual
  • Cleaning of cargo tanks except mandatory prewash
  • Discharge into the sea of tank washings
  • Ballasting of cargo tanks
  • Discharge of ballast water from cargo tanks
  • Accidental or exceptional discharge
  • Control by authorised surveyors
  • Additional operational procedures and remarks

 

Certificates issued under annex 2

Certificate of Fitness Surveys: Initial, Annual, Annual /Intermediate, Intermediate/Annual, Annual & Renewal

 

 

Annex III: Prevention of pollution by harmful substances in packaged form

 

  • Entry into force: 1 July 1992
  • The first of the convention’s optional annexes.  States ratifying the Convention must accept Annexes I and II but can choose not to accept the other three – hence they have taken much longer to enter into force.

 

 

AnnexIII applies to substances listed as marine pollutants in the IMDG code:

 

  • Annex III contains general requirements for the issuing of detailed standards on packing, marking, labelling, documentation, stowage, quantity limitations, exceptions and notifications for preventing pollution by harmful substances.
  • No dangerous goods to be carried by the ships unless a marine pollutant or a dangerous goods declaration has been issued to the master
  • Any dangerous goods carried onboard should be detailed in a stowage plan
  • Packaged goods shall not be accepted unless they are properly marked
  • No packaged goods to be carried unless the ship has an cargo securing manual

 

 

 

Annex IV: Prevention of pollution by sewage from ships

Sewage means

  • Drainage and other wastes from any forms of toilets and urinals
  • Drainage from medical premises ,wash tubs and scuppers located in these premises
  • Drainage from spaces containing living animals

and other waste waters mixed with drainage as above

 

Regulation 10: Standard discharge connections

OD: 210 mm

ID: as per pipe OD

Bolt dia: 17mm

Slots in flange: 4 hole 18mm

Flange thickness: 16mm

Bolts and nuts: 4 x 16mm

 

 

REGULATION 11: DISCHARGE OF SEWAGE

 

Discharge of sewage into the sea is prohibited except when,

  1. The ship is discharging comminuted and disinfected sewage using a system approved by the organization at a distance of 3 nautical miles from the nearest land and that which is not comminuted or disinfected at a distance of 12 nautical miles from the nearest land

 

  1. Sewage shall not be discharged instantaneously, but at a moderate rate when the ship is enroute and doing a speed of not less than 4 knots.

 

  1. Ship has in operation a sewage treatment plant or an approved sewage comminuting and disinfecting system with storage tank or a holding tank of adequate capacity certified by the organization,

 

  1. Test results of the plant are laid down in the INTERNATIONAL SEWAGE POLLUTION PREVENTION certificate. The validity of this certificate shall not exceed more than 5 years.

 

  1. It should not cause any discoloration of the surrounding waters nor produce visible floating solids

 

 

Certificates issued under Annex IV:

 

International Sewage Pollution Prevention Certificate

Surveys: Initial & Renewal

 

Annex V: Prevention of pollution by garbage from ships

  • Entry into force: 31 December 1988
  • Garbage means all kind of domestic and operational waste other than fish, generated during the normal operation of the ship.

 

The entries to be made in the garbage record book

Entries to be made are as follows:

  • When garbage discharged at sea
  • When Discharged at port
  • When incinerated
  • Accidental discharge

 

 

REGULATION 9:  Garbage management plans

Every ship more than 12m or more in length shall display placards  which notify the crew and passengers for the disposal requirements of regulations. The placards shall be written in the working  language of the shall also be English, French ,or Spanish.

  1. Every ship of 400 gt and above and every ship which is certified to carry 15 persons shall carry a garbage management plan. This plan shall have written procedures for collecting, storing, processing and disposing of the garbage including the use of the equipment onboard.
  2. Every ship of 400 gt and above and which is certified to carry 15 persons should have a GARBAGE RECORD book

 

 

CATEGORY OF GARBAGE

  1. Plastics, B. Food wastes, C. Domestic Wastes, D. Cooking Oil, E. Incinerator ashes, F. Operational wastes, G. Cargo residues, H. Animal Carcass(es),
  2. Fishing Gear

 

For a long while, many people believed that the oceans could absorb anything that was thrown into them, but this attitude has changed along with greater awareness of the environment. Many items can be degraded by the seas – but this process can take months or years, as the following table shows:

 

Time taken for objects to dissolve at sea

Paper bus ticket

2-4 weeks

Cotton cloth

1-5 months

Rope

3-14 months

Woollen cloth

1 year

Painted wood

13 years

Tin can

100 years

Aluminium can

200-500 years

Plastic bottle

450 years

Source: Hellenic Marine Environment Protection Association (HELMEPA)

The MARPOL Convention sought to eliminate and reduce the amount of garbage being dumped into the sea from ships.

 

 

 

Simplified overview of the discharge provisions of the revised

MARPOL Annex V which entered into force on 1 January 2013

 

DISCLAIMER: Additional requirements may apply.

 

This simplified overview is for information or reference purposes only and is not meant as a substitute for the comprehensive provisions in the revised MARPOL Annex V (resolution MEPC.201(62)) or the

2012 Guidelines for the Implementation of MARPOL Annex V (resolution MEPC.219(63)).

 

 

 

 

 

Type of garbage

 

 

 

Ships outside special areas

 

 

 

Ships within special areas

 

 

Offshore platforms

and all ships within 500 m of such platforms

 

Food waste comminuted or ground

Discharge permitted

≥3 nm from the nearest land

and en route

Discharge permitted

≥12 nm from the nearest

land and en route

 

Discharge permitted

≥12 nm from the nearest land

 

Food waste not comminuted or ground

Discharge permitted

≥12 nm from the nearest land and en route

 

 

Discharge prohibited

 

 

Discharge prohibited

 

Cargo residues1 not contained in wash water

 

 

 

Discharge permitted

≥12 nm from the nearest land

and en route

 

 

Discharge prohibited

 

 

Discharge prohibited

 

Cargo residues1

contained in wash water

 

Discharge only permitted in specific circumstances2 and ≥12 nm from the nearest

land and en route

 

 

Discharge prohibited

 

Cleaning agents and additives1 contained in cargo hold wash water

 

 

 

 

 

Discharge permitted

Discharge only permitted 2

in specific circumstances

and ≥12 nm from the nearest land and en route

 

 

Discharge prohibited

 

Cleaning agents and additives1 contained in deck and external surfaces wash water

 

 

Discharge permitted

 

 

Discharge prohibited

Carcasses of animals carried on board as cargo and which died during the voyage

 

Discharge permitted

as far from the nearest land as possible and en route

 

 

Discharge prohibited

 

 

Discharge prohibited

 

All other garbage including plastics, domestic wastes, cooking oil, incinerator ashes, operational wastes and fishing gear

 

 

 

Discharge prohibited

 

 

 

Discharge prohibited

 

 

 

Discharge prohibited

 

 

Mixed garbage

 

When garbage is mixed with or contaminated by other substances prohibited from discharge or having different discharge requirements, the more stringent requirements shall apply

 

1      These substances must not be harmful to the marine environment.

 

2       According to regulation 6.1.2 of MARPOL Annex V, the discharge shall only be allowed if: (a) both the port of departure and the next port of destination are within the special area and the ship will not transit outside the special area between these ports (regulation 6.1.2.2); and (b) if no adequate reception facilities are available at those ports (regulation 6.1.2.3).

 

 

Annex VI: Prevention of  Air Pollution from Ships

Adoption: September 1997
Entry into force: 19 May 2005

Emission Gases from Ships

  • Oxides of Nitrogen (NOx) – create Ozone
  • Sulphur Oxides (SOx) – create acidification
  • Carbon Dioxide (CO2) – is a GHG
  • Carbon Monoxide (CO)
  • Hydrocarbons (HC) – gas, soot and some particulates

 

  • AIR POLLUTION PREVENTION
    IMO and Regional Ship Air Emission Developments (cont.)
    • Baltic Sea – SECA from May 2006                                      
    •   North Sea/English Channel– SECA from Nov 2007
               – Major Revision of  MARPOL Annex VI completed in Oct 2008
               – Revised Annex VI effective from 1 July 2010
    •   European Sulphur Directive governing emissions in port                
        (0.1% S at berth 1 Jan 2010)
    •   Port regulations in California (USA), Vancouver (Canada) for ship berthing The California Air Resources Board (CARB) adopted the Regulations to reduce emissions from auxiliary diesel engines and diesel – electric engines operated on ocean-going vessels within California waters and 24 nautical miles off the California baseline.

    •   ISO ongoing  work on Marine Fuel Oil specifications
    •   Discussion and development : of on-shore power supply – also called Alternative Marine Power (AMP) or Cold-ironing
    •   Green House Gases (GHG) limitations
  • MARPOL ANNEX VI applies to all ships but the certification requirements are depending on size of the vessel and when it is constructed.
     
  • Annex VI has requirements to the following main issues:
     Regulation 12 – Emissions from Ozone depleting substances from refrigerating plants and fire fighting equipment
    Regulation 13 – Nitrogen Oxide (NOx) emissions from diesel engines
    Regulation 14 – Sulphur Oxide (SOx) emissions from ships
    Regulation 15 – Volatile Organic Compounds (VOC) emissions from cargo oil tanks of oil tankers
    Regulation 16 – Emissions from shipboard incinerators

Regulation 17- Reception facilities

Regulation 18 – Fuel Oil quality.
 

  • MARPOL Annex VI and the Technical Code have retroactive requirements for the following:

    Regulation 12 – Emissions from Ozone depleting substances from refrigerating plants and fire fighting equipment

    On all ships constructed on or after 19.05.2005.
    Annex VI prohibits any deliberate emissions of ozone-depleting substances. Ozone-depleting substances , and equipment containing such substances, shall be delivered to appropriate reception facilities when removed from a ship. Installations which contain ozone-depleting substances, other than hydrochlorofluorocarbons, are prohibited
     
    Installations containing hydrochlorflourocarbons (HCFCs) are prohibited on ships constructed on or after 1.01.2020.

  • For the ships under regulation 12 of Marpol Annex VI, a list of equipment containing ozone depleting substances shall be maintain and in case a ship will have rechargeable systems containing ozone depleting substances, an Ozone depleting Substances Record Book shall be maintained on board.
     
    The use of Halon in fire extinguishing systems and equipment is already prohibited for new buildings. For new buildings, this requirement in Annex VI will therefore always be complied with. More restrictive requirements for ozone depleting substances are in place regionally, e.g. in the European Union (EU).

 

Vessels carrying ozone depleting substances (ODS) shall maintain a ozone record book. Entries to be made in terms of mass of substance. Entries should be as follows:

  1. Recharge (full or partial) of equipment containing ODS
  2. Repair or maintenance on equipments containing ODS
  3. Discharge of ODS deliberate or non delibrtae
  4. Discharge of ODS to land based reception facilities
  5. Supply of ODS to ships

 

 

 

  • Regulation 13: Nitrogen Oxide (NOx) emissions from diesel engines

    Regulation 13 shall apply to: 

    – Each diesel engine with a power output of more than 130 kW which is installed on a ship constructed on or after 1 January 2000.
     – Each diesel engine with a power output of more than 130 kW which undergoes a major conversion on or after 1 January 2000.
     – Each diesel engine with a power output of more than 5000 kW and a per cylinder displacement at or above 90 litres which is installed on a ship constructed on or after 1 January 1990 but prior to 1 January 2000.

  • This regulation does not apply to:
    – Emergency diesel engines, engines installed in life boats or for any equipment intended to be used solely in case of emergency.
    – Engines used solely to drive machinery dedicated to exploration, exploitation and associated offshore processed of seabed mineral resources The phrase “major conversion”, means a modification of an engine where:
    The engine is replaced by a new engine built on or after 1 January 2000, or
    2. Any substantial modification is made to the engine, as described in the Nox Technical Code 1.3.2 (e.g. changing camshaft,fuel injection system, or any other NOx-related settings or components), or
     
    3. The maximum continuous rating of the engine is increased by more than 10% For this purpose, Substantial Modification is defined as follows:
     
  • For engines installed on vessels constructed on or after 1 January 2000, a Substantial Modification means any modification to an engine that could potentially cause the engine to exceed the emission standards set out in Regulation 13 of Annex VI.
  • For engines installed on vessels constructed before 1 January 2000, a Substantial Modification means any modification made to an engine which increases its existing emission characteristics established by the simplified measurement method as described in 6.3 in excess of the allowances set out in 6.3.11(Ref. NOx Technical file.). These changes include, but are not limited to, changes in its operations or in its technical parameters (e.g. changing camshaft,fuel injection systems, air systems, combustion chamber configuration, or timing calibration of the engine)

 

 

 

 

  • Regulation 13 contains further a 3-Tier approach as follows:

     Tier I (current limits)
    For diesel engines installed on ships constructed from 1 January 2000 to 1. January 2011 allowable emissions of total weighted NOx depending on engine speed, n, are:
    17,0 g/kWh when n is less than 130 rpm
    ii. 45,0 × n(-0,2) g/kWh when n is 130 or more but less than 2000 rpm
    iii. 9,8 g/kWh when n is 2000 rpm or more

    Tier II
    For diesel engines installed on ships constructed on or after 1 January 2011 allowable emissions of total weighted NOx depending on engine speed, n, are:
    i. 14,4 g/kWh when n is less than 130 rpm
    ii. 44,0 × n(-0,23) g/kWh when n is 130 or more but less than 2000 rpm
    iii. 7,7 g/kWh when n is 2000 rpm or more

 

 

Tier III
Ships constructed on or after 1 January 2016 will have additional limitations when operating in an Emission Control Area.
For Tier III ships operating in the NOx ECAs the allowable
emissions of total weighted NOx depending on engine speed, n, are:
i. 3,4 g/kWh when n is less than 130 rpm
ii. 9,0 × n(-0,2) g/kWh when n is 130 or more but less than 2000 rpm
iii. 2,0 g/kWh when n is 2000 rpm or more

 

  • The NOx-influencing components and settings depend on the design of the particular engine, and shall be listed in the engine’s Technical File. The below list shows typical NOx-influencing parameters, but are not limited to:
    Injection timing
    2. Injection system components (nozzle, injector, fuel pump)
    3. Software no, checksums, or other identification of software version
    4. Hardware for fuel injection control
    5. Camshaft components (fuel cam, inlet- and exhaust cam)
    6. Valve timing
    7. Combustion chamber (piston, cylinder head, cylinder liner)
    8. Compression ratio (connecting rod, piston rod, shim, gaskets)
  1. Turbocharger type and build (internal components)
    10. Charge air cooler/charge air pre-heater
    11. Auxiliary blower
    12. NOx reducing equipment “water injection”
    13. NOx reducing equipment “emulsified fuel” (fuel/water emulsion)
    14. NOx reducing equipment “exhaust gas recirculation”
    15. NOx reducing equipment “selective catalytic reduction”

    The actual Technical File of an engine may include less components and/or parameters other than the list above, depending on the particular engine and the specific engine design.

       
The NOx emissions at Tier I level upgraded for engines of power output > 5,000 kW and per cylinder displacement at or > 90 litres

The upgrading is provided with approved and cost effective method for NOx limitation and should not:
– reduce the engine rating by more than 1%
– increase the fuel consumption by more than 2%, and
– have negative effect on the engine durability or reliability

 

For Engines NOT complying with Tier I NOx emission limitations:
•   measures against ship only if there is a certified, efficient commercially
     available system
•   rules for certification, verification and documentation of scrubbers
    and upgrade at the ship’s first Renewal Survey if there is an approved
    method for upgrading at least to Tier I standard
•   if system not available, the next Annual Survey after that method is available

 

  • NOx Reduction Options:

 

For  existing  engines:
• Use of NOx injectors
• Retarding injection timing
• Temperature control of the charge air
• Exhaust Gas Recirculation (EGR)
• Fuel / water emulsion
• Water injection
• Humid Air Motor (HAM) Technique- addition of wet steam
to the engine
• Selective Catalytic Reduction (SCR)

 

 

 

 

For new engines:
Engine certification
– Pre-certification,
– Technical file clarification on engine family and group,
– Final certification

  • Regulation 13 requirements are fully defined by the NOx Technical Code – recommended technical reading.
    – Certification of the engine on manufacture and checked on installation for settings
    – Certificates required for Ships – EIAPP & IAPP
    – PSC Inspection of the engine by
    Parameter Check method (Engine Technical File)
                    ii. Simplified measurement method

 

  • Regulation 14 – Sulphur Oxide (SOx) emissions from ships
    – 19 May 2005 Annex VI to MARPOL entered into force.
    – The revised Annex VI to MARPOL was adopted by IMO on 10 October 2008.

    The sulphur oxide (SOx) and Particulate Matter emissions from ships will in general be controlled by setting a limit on the sulphur content of marine fuel oils as follows. The sulphur content of any fuel oil used on board ships shall not exceed the following limits:

* depending on the outcome of a review, to be concluded in 2018, as to the availability of the required fuel oil, this date could be deferred to 1 January 2025.

SOx: Relates to the emission due to the sulphur content in the fuel

 

  • Under the revised MARPOL Annex VI, the global sulphur cap is reduced initially to 3.50% effective from 1 January 2012
  • Then progressively to 0.50% effective from 1 January 2020.
  • The limits applicable in ECAs for SOx and particulate matter were reduced to 1.00%, beginning on 1 July 2010
  • Being further reduced to 0.10 %, effective from 1 January 2015.
  • As per EU directives the limits applicable are 0.10% in EU ports

 

 

Outside an ECA established to limit SOx and particulate matter emissions

Inside an ECA established to limit SOx and particulate matter emissions

 

4.50% m/m prior to 1 January 2012

 

1.50% m/m prior to 1 July 2010

 

3.50% m/m on and after 1 January 2012

 

1.00% m/m on and after 1 July 2010

 

0.50% m/m on and after 1 January 2020*

 

0.10% m/m on and after 1 January 2015

 

Emission Control Area, ECA:

Means an area where the adoption of special mandatory measures for emissions from ships is required to prevent, reduce and control air pollution from NOx & SOx & particulate matter.

 

  1. The ECA established are:
    Baltic Sea area – as defined in Annex I of MARPOL (SOx only);
    ii. North Sea area – as defined in Annex V of MARPOL (SOx only);
    iii. North American area (entered into effect 1 August 2012) – as defined in Appendix VII of Annex VI of MARPOL (SOx, NOx and PM); and
    iv. United States Caribbean Sea area (expected to enter into effect 1 January 2014) – as defined in Appendix VII of Annex VI of MARPOL (SOx, NOx and PM).

 

  • Most ships which operate both outside and inside these ECA will therefore operate on different fuel oils in order to comply with the respective limits. In such cases, prior to entry into the ECA, it is required to have fully changed-over to using the ECA compliant fuel oil, regulation 14.6, and to have onboard implemented written procedures as to how this is to be undertaken. Similarly change-over from using the ECA compliant fuel oil is not to commence until after exiting the ECA. At each change-over it is required that the quantities of the ECA compliant fuel oils onboard are recorded, together with the date, time and position of the ship when either completing the change-over prior to entry or commencing change-over after exit from such areas. These records are to be made in a logbook as prescribed by the ship’s flag State, in the absence of any specific requirement in this regard the record could be made, for example, in the ship’s Annex I Oil Record Book.

 

  • Sox Control:
    – Arrangements for LSFO & HSFO: 2 0r more different types of fuels.
    Availability: Bunking strategies
    Switch-over: (12 to 24 hrs) will need to be changed over the fuel for the SECA passages.
    Handling of cylinder oils: 2 qualities may be required.
    – More strict follow up through sample requirements, and control of documentation and procedure to log down.

 

Other Methods for Controlling of Nox and Sox:
– Exhaust gas cleaning system or other equivalent system: May be used (abatement technologies). The emission criteria for such systems are 6 g SOx/kWh.
 – Relifiquation plants for LNG/LPG carriers:  Reduction of NOx, Sox & cost saving through boiled off gas reuse.
– Alfa Lubricator system: Reduction in cylinder oil consumption. Reduction in particulate emission.
– Electronic control engine: Programmed fuel injection and exhaust valve. Reduce fuel & reduction of emission.
– Turbo generator plant: Use of high efficiency air flow for power take off. Reduce fuel & reduction of emission.
– System integration: Humid air Motor (HAM)- engine intake air operating with water & exhaust gas recirculation (EGR). 50% reduction of emission.
– HFO sulfur content – Use of low sulfur oil and modify the equipments to burn LSFO.
– Dual fuel option for low sulphur restricted areas: Need for additional tanks and dual fuel engines.

 

Regulation 15 – Volatile Organic compounds emissions from cargo oil tanks of oil tankers

  • Subject to individual terminal regulations tankers may have to be equipped with Vapour return manifold.
  • Notification of VOC control by a port to the IMO shall be 6 months before enforcement.
  • Tankers can be can accept tankers upto 3 years after the date of VOC control enforcement by the Terminal.
  • The standard for the design of VOC return manifold and operation is contained in MSC/Circ.585

 

Regulation 16 – Emissions from shipboard incinerators

  • Incinerators installed after 1st Jan 2000 to meet regulations and must certified to meet the specifications in MEPC Resolution 76(40) (Appendix IV of Annex VI).
  • Each incinerator must have a manufacturers operations manual.
  • Crew responsible for the incinerator operation shall be trained and follow the operations manual.
  • The following substances are prohibited from incineration:
    • Annex I, II and III cargo residues and related packing material.
    • Garbage as defined by Annex V containing heavy metals.
    • Petroleum Products containing halogens.
  • PVC can only be incinerated in type approved incinerators.
  • Flue gas temperatures shall be monitored and not less than 850 deg C for continuous feed and reach 600 deg C within 5 minutes for batch feed.

 

 

Regulation 17 – Reception Facilities
 
•  Parties obliged to provide facilities without causing delay for:
– Reception of ODS in ship repair yards (Reg.17.1.1)
– Reception of Exhaust Gas Cleaning System residues (Reg.17.1.2)
•  Reception of ODS in ship breaking facilities (Reg.17.1.3)
•  If unable to provide reception facilities then Party shall inform IMO (Reg.17.2 & 17.3)

 

Regulation 18 – Fuel Oil quality.

  • “Fuel oil shall be blends of hydrocarbons derived from petroleum refining”
  • “Fuel oil shall be free from inorganic acid”
  • “Fuel oil shall not include any added substance or chemical waste which either:

– Jeopardises the safety of ships or adversely affects the performance of the machinery, or

– Is harmful to personnel, or

– Contributes overall to additional air pollution”

 

Bunker Delivery Note (BDN):
– Becomes a Statutory document
– Must be kept on board for 3 years for inspection and a copy may be taken for further examination by PSC.
– Must contain all data required by Appendix V
– Name and IMO number of vessel Port
– Date of Commencement of delivery
– Details of fuel oil supplier
– Product name, quantity , Density at 15 0C and Sulphur content % m/m
– A declaration that fuel supplied meets Regulation 14 and 18 requirements

 

Fuel Oil Sampling
– A sealed sample meeting the requirements in associated guidelines has to supplied to the ship by the bunker supplier
– For each individual BDN a sample has to be taken at the vessel’s bunker receiving manifold. (see procedure in associated guidelines) – ISM  Manuals.
– The sample label has to be signed by both the bunker supplier’s representative and the vessel’s Chief Engineer.
– The sample size shall be not less than 400 mls
– The sample is not to be used for any commercial purpose
– The sample is to be retained on board for at least 1 year for inspection by PSC as required

 

Shipboard Procedures for  BDN and Samples

  • Adequate bunker manifold location for sampler attachment
  • External safe storage location for samples for 1 year period
  • Log book for sample retention and custody transfer
  • Safe storage for BDNs and other documents relating to bunkering onboard
  • Port/Flag State Control Guidelines
  • Proposed Guidelines from FSI 13 for MEPC 53 approval.
  • Initial inspections and Primary survey parameters – then “Clear Grounds” for

     in-depth inspections

  • “In depth” inspection parameters
  • Detainable deficiencies
  • Non-Party ship inspections

 

Port/Flag State Control  Guidelines

Parties are required to:

– inform the Party or non-Party under whose jurisdiction the BDN was issued in cases of delivery of non- compliant fuel oil (Reg.10.1)

– ensure non-compliant fuel oil is brought into compliance (Reg.10.2)

  • For ships on scheduled services with frequent and regular port calls Administration can provide alternative procedure to retaining on board BDN (Reg.11)

 

Enforcement – port State control

  • Resolution MEPC.181(59) adopted 17 July 2009
  • Identifies key compliance issues:

– Documentation – IAPP, EIAPP, BDN’s

– Compliance with SOx limits – fuel record book/EGS

– Compliance with engine limits for NOx

– Compliance with ODS provisions – ODS record book

– VOC management plan (if required)

– Type approval certificate for incinerator

 

 

Certificates issued under MARPOL Annex VI

 

International Air Pollution Prevention Certificate with supplement with details on the above 5 criteria

Surveys: Initial, Annual, Annual /Intermediate, Intermediate/Annual, Annual & Renewal

 

International Energy Efficiency certificate

Shipboard Energy Efficiency Management Plan

 

  • Ships of 400 gross tons and above engaged in international voyages involving countries that have ratified the conventions, or ships flying the flag of those countries, are required to have an International Air Pollution Prevention Certificate (IAPP Certificate).
     The IAPP certificate will be issued following an initial survey carried out by the Flag Administration or by the Class (e.g. DNV, ClassNK) on behalf of the Flag Administration, confirming compliance with MARPOL Annex VI. For ships with the flag of an Administration that have not yet ratified Annex VI, a Certificate of Compliance with Annex VI issued by the Class.

 

  • Annex VI also requires diesel engines (as described above) to carry individual certificates with regard to NOx emissions, named Engine International Air Pollution Prevention (EIAPP) Certificates.
    Annex VI requires that every ship of 400 gross tonnage or above and every fixed and floating drilling rig and other platforms shall be subject to the surveys.

 

Surveys:
 – An initial survey before the ship is put into service or before the IAPP Certificate is issued for the first time.
Periodical surveys at intervals specified by the Administration, but not exceeding five years.
– A minimum of one intermediate survey during the period of validity of the certificate.

Renewal survey to revalidate the certificates before expiry. 

In the case of ships of less than 400 gross tons, the Administration may establish appropriate measures in order to ensure that Annex VI is complied with.