Author Archives: Mohammud Hanif Dewan

UMS SYSTEM FAILURE

(By Kamal Hossain, Chief Engineer)

It is complete failure of the UMS, bridge control and data logging system has failed and the main engine is needed to run on manual control and monitoring.
(a) State with reasons six main items of data, which require to be monitored and recorded manually.
(b) Explain how a watch keeping system should be arranged to provide for effective monitoring and control of the main engine.
(c) Explain how the staff will be organized to maneuver the engine safely. State the machinery plants at which attentions are required during maneuvering.

Answer:

(a) When M.E to be put on manual control and monitoring, the following six main items of data to be monitored and recorded manually.

1. Cooling water system.
It is required to prevent the thermal stress and thermal loading on the engine. Engine may breakdown in severe
Case.
– Jacket water temperature and pressure
– Piston cooling temperature and pressure ( If water cool )
– Sea water temperature and pressure ( For Coolers & condenser ) …. to be checked & recorded.

2. Lubricating oil system
It is required to prevent thermal stress, occurrence of hot spot, local welding between engaging aspirate and seizure case for severe condition. It is also reducing the wear and tear in engine component .
– Lub. Oil pressure & temperature for crankshaft bearings & camshaft bearings
– Cylinder Lubrication
– T.C Lubrication……… to be checked and recorded.

3. F.O system
It is required to obtain the correct fuel injection viscosity to achieve good combustion process in the cylinder.
– Fuel oil pressure at circulation system
– Fuel oil temperature at end heater
– Fuel oil viscosity at visco-therm unit
– Condition of fuel oil settling and purification process… to be checked and recorded.

4. Scavenging & Exhausting
It is required to know the engine’s load distribution, combustion condition, exhaust valve condition, turbocharger efficiency and charge air cooler condition.
– Charge air temperature and pressure
– Air cooler in / out temperature
– Individual unit’s exhaust temperature
– Turbine inlet & outlet temperature………….to be checked and recorded.

5. Level control
It is required to checked and maintained the correct level of
– Boiler water level for safe running with correct steam pressure
– Cooling water expansion tank level
– Fuel oil settling and service tank level
6. Speed and revolution counter
It is required to monitored and recorded running machinery speed and revolution counter, to determine the engine
performance with respect to exhaust temperature and load condition.
– M.E r.p.m
– Turbocharger r.p.m

(b) Monitoring & Control

To obtain effective monitoring and control of main engine, E.R attend watch keeping to be provided instead of UMS system. In every watch , one certified Engineer in full charge and at least one assistant should be performed. Watch keeping should be 3 shifted as follow :
– 00 ~ 04 and 12 ~ 16 watch 2/E + one assistant
– 04 ~ 08 and 16 ~ 20 watch 1/E + one assistant
– 08 ~ 12 and 20 ~ 24 watch C/E + one assistant
Overtime could be assigned for 2 hour each after completion of day time watch keeping.
Electrician , Fitter and remaining crew ( if any ) to be assigned day work ( Normally 0700 ~ 1600 )

In the watch hour, watch keepers must keep the close watch to monitor and maintain all temperature and pressure of the running machinery. All data to be collected and entered to Chief Engineer’s log book 4 hourly .

(c) Organization to Engine room staff (for safe maneuvering)

When M.E running with manual control and monitoring , there should be full strength of E.R crew to present in E.R for safe manoeuvring. In addition to present watch keeper, stand-by Engineer and day work crew must present in E.R when engine is given stand-by notice. In the manoeuvring period, the followings to be assigned.

– As a Chief Engineer, he is a responsible person in full charge in E.R
– Duty Engineer should take engine movement control.
– Standby Engineer should keep close watch in engine room’s machinery and maintain all temperature and pressure within normal limit.
– Electrician should be standby for main switch board and help to record engine’s movement.
– Assistant watch keeper should take care of air compressor and fuel centrifuging.
– Fitter and day work crew should attend in M.E individual platform, check engine movement and stand-by for emergency case.
The following machinery plants are required to pay attention during maneuvering.

– M.E warming All temperature and pressure to be maintained within normal limit while manoeuvering period.

– Generator plant : Require two generator in parallel operation to sufficient manoeuvring loads. If not satisfactory standby generator must be running idle for emergency.
Emergency generator room to be clearly opened and keep ready.

– Air compressor plant Attention to pay air compressors and air reservoirs . Alert to change air bottle if air pressure drop to minimum starting level.
– Fuel Centrifuging Normally, Diesel oil is used for manoeuvring. Therefore check D.O service tank level and topping up as necessary.
– Boiler plant E.G boiler may not sufficient to produce required steam pressure. Therefore aux. oil fired boiler have to put in service. Correct firing procedure and its safety measures to be watched.

– Steering gear Keep watch its proper function . Alert to change emergency operation in case.

CHIEF ENGINEER RESPONSIBILITIES DURING BUNKERING OPERATION

(By Kamal Hossain, Chief Engineer)

Pollution prevention

    1. Pre-bunkering meeting should be held , quantity , grade and distribution plan to be drawn up.
    2. By considering of volume allowance is 10 ~ 15 % for expansion , all tanks to be filled up to 85 % maximum.
    3. Clear over flow tank , drain tank .
    4. Top up settling and service tanks.
    5. Clean filters and sight glass of bunker line.
    6. Keep level indicator, sounding gauge and pressure gauge good working order.
    7. Arrange quick communication between bunker point and control .
    8. Check scuppers plug condition.
    9. Keep cleaning materials and chemical near by bunker point.
    10. Alert oil pollution control team as per contingency plan.

 

  1. Exact reading of draught and list to calculate trim of the ship. Keep vessel up right as possible.
  2. All tanks to be sounded priorly.
  3. Check valve opening to correct tank and others shut.
  4. Predetermine the pumping rate and emergency stop signal with supply barge.
  5. Pumping slowly during first stage , check oil enter to correct tank , hose connection especially on the non-used side, then increase to predetermined pumping rate.
  6. Check sounding of filling tanks frequently , use ullage method.
  7. Regular check for oil trace from connections and ship side discharge . If any leak is found , stop bunker immediately.
  8. Essential to slow down when 80 % of total quantity and to be stopped at 85%.
  9. Let all valves open for some duration to expel the air from tank.
  10. Avoid spillage when connecting or disconnecting the hose.

U.S.C.G Regulations

  1. Bunker plan must be drawn up . All crew to be explained total bunker quantity , distribution plan , filling sequences. Engine room staffs to be assigned each and individual duties regarding bunker. This plan and assignments must be posted at bunker point.
  2. All bunker tanks must have vent pipes with flame trap head and spilled oil container of 1 Barrel Quantity to be placed near vent pipes.
  3. Chief Engineer must prepare necessary paper forms and to be signed prior to bunker as per procedures to regulations.

Fire Prevention

  1. Bunker oil flash point must not be less than 65’C under any circumstance as a rule.
  2. Ensure no oil leakage.
  3. No naked light or smoking is allowed in the vicinity.
  4. Keep fire stand-by watch with portable fire extinguishers.

How to minimize the shortage.

  1. Take exact reading of draughts and list to calculate trim of the ship. Keep vessel up right as possible.
  2. All tanks to be sounded . Calculate on board balance condition and plan the distribution.
  3. Avoid mixing the bunker from different origin.
  4. Check specifications of bunker , temperature , flash point , viscosity , specific gravity ,…. ect., according to delivery order.
  5. Take soundings of bunker barge using water finding paste .
  6. Record time of commence and completion , pumping rate .
  7. Take final soundings of total bunker by using water finding paste  , calculate receiving amount of bunker by using volume correction factor as per A.P.I  and gravity with exact temperature.
  8. Call bunker surveyor through agent for any dispute.

After bunker

  1. Take 3 sample bottle , one for ship , one for analysis and another for bunker supplier. All samples to be sealed ,with both ship and barge ‘s stamps , date , place and signs of Chief Engineer and supplier.
  2. Check delivery receipt , describing amount and specifications to be the same with delivery order. Then chopped and signed. At least 2 copies of receipt to be kept for ship. One for F.O report to Head Office and one for ship file.
  3. Log to be enter official and actual receipts. B.O.B at this moment to be mentioned. Inform bridge.
  4. Oil Record Book to be entered with correct code no., item no., date, place, exact time of commence and completion, added  and total quantity of tanks with number, and signed.

How to take sample and requirements.

  1. Sample must be taken by continuous dripping method . The sample to be drawn from bunker line by using of dripping probe or  drain valve crack open for dripping at oil pump out let from barge.
  2. Sample bottle is 1 ltr capacity. If tin container it must be 4 ltr capacity.
  3. Sample oil bottle is to be sealed in front of Chief Engineer or other witness.
  4. On the seal the following to be provided.
  5. Place and date of bunker sampling
  6. Method and place of drawn
  7. Name of barge
  8. Name of ship
  9. Quantity and grade
  10. Name of Chief Engineer and Supplier
  11. Signs of them
  12. Samples to be taken 3 bottle. One for ship , one for analysis and another for supplier.
  13. Sample should be kept on board not less than 30 days from date of bunker receiving or until the bunker is totally consumed.

Bad  Bunker

Bad bunker is caused when taking two different fuel oil within a specifications but a heavy sludge precipitation and not fit for further use. It may effect the Engine the following problems.

  1. High exhaust temperature
  2. Burning exhaust valve
  3. High combustion pressure
  4. Blow by and fire in scavenge
  5. High wear rate of engine parts
  6. Decrease performance
  7. Clogging of fuel system

How to minimize to receive bad bunker

  1. Order to standard marine fuel oil supplying contract
  2. Specifications must be complied with engine maker’s recommendations.
  3. Bunker may be refused if in doubt regarding specifications.
  4. Try not to mix bunker from different origin. Store in a tank having no oil remains.
  5. Proper sample to be drawn , sealed and taken.
  6. Sample to be analyzed by renown company.
  7. Sample to be kept on board till oil is totally consumed.
  8. Try not to burn as possible , before receiving lab report.

How to use bad bunker oil if  No-way

  1. Sludge dispersion chemical to be applied to banker storage D.B and settling tanks.
  2. Applied heating to storage D.B ,settling and daily service tanks at temperature well above its pour point for separation of water and other impurities. Frequent draining practice to be followed.
  3. Use double stage purification method with slow feed rate. ( Purifier & Clarifier in series operation ). Frequent Desludging process to be made. Cleaning of these centrifuges and their filters to be done more than normal routine.
  4. Chemicals to be added in daily service tanks to improve combustion.
  5. Filters in F.O system to be cleaned more than normal routine.
  6. Maximum permissible heating temperature to be applied to gain good viscosity control at visco-therm unit.
  7. In some case , raise the temperature of fuel and charge air temperature 5 ~ 10’C more , it may effective to avoid combustion delay and fuel knocking.
  8. While engine is running with bad fuel, the following factors to be keep close watch, and maintenance to be done:
  • Exhaust temperature
  • Cylinder and piston cooling temperatures
  • F.O line and end heater temperature
  • Visco-therm unit
  • Charge air temperature.
  • Turbocharger r.p.m
  • Multiply the turbocharger water washing practices.
  • Peak pressure indicator to be taken and check the engine condition.
  • Fuel injectors to be cleaned and pressure to be tested

 How to handle and maintain bunker oil

It is necessary to maintain and up grade the critical properties of bunker oil through the ship board process. These are consisting of the followings:

  • Sediments settling process
  • Filtering process
  • Centrifuging process
  • Mechanical process
  • Chemical process.

The procedures for the above process are as follows:

1. Bunkers of different origin are stored in separate D.B. tanks. Coarse filters in bunker line is passed by the bunker oil while bunkering.

2. Heating is applied to storage D.B. tank to keep bunker oil temperature well above pour point and below flash point

3. Detergent type chemical additives should be dosed into the storage D.B. tank to prevent too much sludge formation.

4. Then , transferred the oil by pump with coarse filter, to settling tanks, which are having adequate heating arrangement and designed with slope bottom to improve contaminant draining. In this tanks , oil is settled and applied heating. Gravitational separation of oil from water and other impurities may occur and frequent drainage of them can be done. Oil temperature in this stage is kept not more than 60’C practically.

5. After settling out some water and impurities for about 24 hrs or more, the oil is fed to the separators passing through coarse filters in each unit again.
Double stage separation method by using purifier and clarifier in series with heater is promoting separation effect. All the contaminants and water are separated off during these process and almost clean oil is led to daily service tank which is same designed and arrangements provided as settling tanks.

6. Some firms are making finishing touch process at this point which are include several filters, Ultrasonic or Mechanical Homogenizer and Emulsifiers.

7. At the daily service tanks, by applying heating and maintain oil temperature about 60’C practically gravitational separation occur again. Then some remaining water can be drained out if any. Chemical for combustion improver can be dosed. At this stage , the oil is well processed and ready for use.

8. For burning process, the oil is drawn by booster pump from daily service tank to closed mixing column via coarse filter. From there the circulating pump feed oil to end heater to give correct injection viscosity control by Visco-therm unit. piping from end heater to fuel pump and injectors are provided with heating arrangement, and heated oil is led to pass through back flush filter which having filtering capacity up to 1 micron particles.

EFFECTS OF IMPURITIES IN FUEL OIL

Q. Write brief notes on the adverse effects that a fuel containing high value of the following may cause: (a) Viscosity (b) Density (c) Sulphur (d) Corodson Carbon Residue (e) Asphaltene (f) Vanadium & Sodium (g) Ash (h) Water

(By Kamal Hossain, Chief Engineer)

Viscosity

High viscosity of fuel may cause the following effects being using high temperature heating
– Fouling of Oil heater
– Gassing of Fuel
– Thermal expansion to fuel pump and injector component leading to seizure or sticking
– Clogging of filter

Density

High density of fuel oil means high contents of impurities . It may effect to
– Filter clogging
– High temperature require for sedimentation & purification
– Upsetting to purifiers
– Being fuel pump is volume-measuring device , produce more heat when combustion .

Ash

Natural ash are usually Silicon , Aluminium , Calcium , Iron , Nickle , Vanadium and Sodium . If high ash content may effect the following
– High density
– Defects in filtration and purification
– Deposits may effect as abrasive wear to piston rings , liner , fuel pump components , T.C turbine blades
– Dangerous effect of Vanadium and Sodium may shorter exhaust valve life.

Water

More than 1 % of water content may cause
– Corrosion on fuel pump and injector component tend to seizure.
– Misfiring of engine and stop in extreme case
– Poor combustion , reduce out put and T.C surging
– Emulsification of fuel leading to sludge formation
– Fuel foaming in mixing column
– Promote microbial degradation
– Loss of energy content and quantity of fuel.

Sludge

It may cause
– Instability of fuel
– Blockage of filters
– Upsetting of purifier operation

Asphaltenes

It is a hydrocarbon compound of solid combustible substances which are insoluble in fuel oil. Asphaltenes may cause

– Clogging of filters ,Fouling of heaters and upsetting purifier operation
– Corrosion of fuel pump’s component and seizure
– Sticking of nozzles and tend to trumpet formation
– Prolong combustion time and its flame close to liner wall and overheat , burn cyl. L.O
– Due to poor combustion , unburned products tend to abrasive wear of Piston Rings & Liners , seizure & broken piston rings.
– Fouling of scavenge port and exhaust system

Sulphur

– Produce combustion products containing SO2 & SO3 to cause cold corrosion wear of
Piston rings, Liners ,Turbocharger water cooled casing , Exhaust valve cage….. ect.
– High temperature corrosion to exhaust valve.
– Adhesion of black lacquer on the liner inner surface
– Form L.O acidity condition.

Vanadium,Sodium

May cause hot corrosion during combustion . They are formed corrosive products as SODIUM VANADATE COMPOUND when combustion temperature 530 ‘C , stick to the metal and attack the protective coating of the surface , cause hot corrosion especially to Exhaust valve , Turbocharger turbine blades and nozzle ring.

Carbon residue Poor combustion with smoky exhaust and produce depositing product effect to ….
– Trumpet formation of nozzle
– Depositing Piston ring zone tend to seizure and broken
– Remove cylinder L.O film and act as abrasive to wear Piston rings and liners, – –
– Fouling of scavenge space and inlet / exhaust ports
– Depositing in Turbocharger and corrosion to nozzle ring and turbine blades
– Fouling at Economizer and uptake

Catalytic Fines.

These are very small size of 3 ~ 100 microns, hard and abrasive compound of Alumina and Silica.
Larger parts may increase wear in fuel pump and valve components
Smaller parts below 5 micron promote Piston rings & Liner wear.

SHIP CHARTER

F R Chowdhury

In shipping when a ship is hired it is always referred to as being on charter. The owner of the ship is still referred to as the owner and one who hires the ship or space thereof is referred to as the charterer. The instrument of agreement is known as the “charter party”, commonly called C/P. There are standard forms for different types of charter devised by various international trade associations and chambers of trade and commerce including the ICC, BIMCO and the Baltic Exchange. C/P is normally drawn by mutually (ship-owner and charterer or their agents) agreeing to various clauses of one of the specific forms with special conditions or exception/ exemption noted by lines. The coal, grain rice, timber, stone, ore, fertiliser, and other trades all have their own forms of charter-party. There are 3 conventional types of charter. They are:
1. Demise or Bare-boat charter
2. Time charter
3. Voyage charter

Demise or bare-boat charter:

as the name implies it is the charter in which the charterer hires the ship for a long period of time, mostly in newly built condition directly from the yard, and takes delivery of the ship with no crew, stores or bunkers. In other words the delivery of the ship is made in its bare state. The charterer employs his staff to man the vessel, puts on board stores, provision and spares as considered necessary, takes bunkers, finds cargo and employs the vessel. In most cases the insurance of the vessel may be also undertaken by the charterer. The charterer takes the responsibility of repair, maintenance, survey, certification and docking. The owner has no operational responsibility. The oil companies normally operate the tankers under bare-boat registry (often taken as a new delivery from the yard).

The charterer operates the vessel (in lawful trade) in a manner as if s/he is the owner. The charterer can even put his/ her own marking on the funnel. However, the charterer cannot raise any cash/ finance against the ship because s/he is still not the owner. Some countries also allow registration of a ship under bare-boat charter for the period of charter or if the C/P leads to eventual sale of the ship to the charterer. However, the C/P has to have a clause allowing the charterer to register the ship under a different flag for the period of charter. The Administration of the bare-boat registry will evidently seek the consent of the primary register before the vessel is registered under bare-boat registry.

Time charter:

The ship is chartered for a specific period, say about six months to a year, at a fixed rate (normally a daily rate) with option to extend the period to complete a voyage. On mutual consent the charter may be renewed or extended for further period. Charter hire is normally paid in advance, say about 15 or 30 days at a time. The owner retains the master and the crew and continues to pay their wages. The owner continues to pay for the insurance (hull and machinery and P&I for the crew). The charterer may take a P&I cover for cargo or other claims. There are special charterers’ P&I clubs to provide coverage of the charterers’ requirements. The owner also remains responsible for repair, maintenance, survey and certification. The vessel is normally put “off-hire” for the period vessel becomes/ remains non-operational.

The charterer finds the cargo and employs the vessel. He pays for fuel, pilotage and port dues. He also pays for stevedoring, dunnage, lashing, tomming etc., if any. The charterer or his agents issues the B/L (Bill of Lading). If the master is required to sign the B/L he does so “for and on behalf of the charterer”. The owner who also pays for the fresh water consumed by the crew pays lubricating oil, being a part of the ship’s maintenance. The charterer may put its own marking on the funnel.

Normally there is “on-hire” and “off-hire” survey at the time of delivery/ re-delivery to ensure that the ship is returned to the owners in the same state as was chartered. Compensation is paid for any damages caused during the charter. Differences in the quantity of oil and water are normally settled at the rate prevailing at the port of re-delivery. The owners pay for crew (for routine operation and maintenance) but any over-time for the business of the charterer is paid for by the charterer.

The master abides by and carries out all lawful advice and instruction of the charterers. Charterer’s representative or Cargo Superintendent may be allowed to stay on board for which the owners may claim boarding expenses. Entertainment (hospitality) expenses in respect of pilot, port officials, customs etc. are reimbursed by the charterers.

There are also trip time charters, which are for shorter durations related to one specific voyage between two or more ports. The principle remains the same as long term time charter parties.

Voyage charter:

It is in fact an agreement between the owner (carrier) and the charterer (shipper) to carry a given quantity of cargo from a point A to a point B at an agreed rate of freight per ton. It normally refers to a quantity with +/- 2% option for either party. The ship will serve “Notice of Readiness” on arrival at loading port when it is ready for loading. If it is on liner terms the owner (carrier) employs stevedores at both ends and pays for it. However, the charterer must provide the cargo to the hook for loading and away from the hook at the port of discharge. However, in most voyage charter the loading and discharging is done by the charterer. The C/P will stipulate either on FIO (free in out) or FIOST (free-in-out, stowed and trimmed) basis and the rate at which the loading and discharging will be done by the charterers. If stipulated in the C/P the ship may give notice of arrival at the port of discharge to charterer and the charterer’s agents may handle the ship.

The C/P stipulates a given rate of loading/ discharging (time factor) and if the charterer fails to maintain the flow at the given rate and causes delay to the ship then demurrage is payable by the charterer to the owner at a pre agreed rate. Similarly if the charterer handles the ship at a rate faster than stipulated and thereby releases the ship ahead of schedule then the owner pays to the charterer “despatch” money which is normally fixed at a rate lower than the demurrage. Generally it is fifty percent or half of the agreed demurrage rate.

In voyage charter the owner meets all expenses relating to the ship and its operation. The charterer pays for the cargo carried at the agreed rate.

Bulk import by state owned organisations through tender/ quotation normally invite bids for a certain quantity of a specific cargo (normally import) to be delivered to a point at an agreed rate. This involves for the supplier to buy the goods and ship it through voyage charter. The ship is required to serve notice of readiness and the importer (consignee) will take delivery of the goods at a stipulated rate of discharge with provision for demurrage. If a B/L is required for banking purpose then it is signed with a clause “all terms and conditions as per C/P”.

It is quite possible for the same ship to be first on bare-boat charter with one party, time charter with a second party and then finally on a voyage charter or liner engagement. In modern global shipping there is also charter for space or slot charters.

NYPE and GENCON:

NYPE and GENCON charter parties are most frequently used for time and voyage charters respectively. These are standard forms which have undergone many revisions. There are also many bespoke (tailor made) charter parties for genre specific shipments. BIMCO is one of the major organisations which introduce specific Rider Clauses to Charter Parties, depending upon the frequent changes to shipping trade. The Piracy Clause is one such example of a new introduction since the Somalian Piracy operations created problems with shipping routes.

Disputes and Arbitration:

Like every contract, Charter Parties may also have their usual disputes. Resolving these is through an appropriate Clause such as the Arbitration Clause. The most frequent place agreed is in London with English law to apply. Arbitrators are generally members of the LMAA. The arbitrators “award” is often accepted as a solution to the dispute. There are however a good number of these being challenged at the court of First Instance with further appeals working its way up to the House of Lords where major maritime cases are discussed and judgments are issued. These form the back bone of English Maritime Law.

The Ship Broker:

The intermediate party to drawing up a Charter is the ship broker, who is the common party to the Owner and the Charterer. Reputable brokers are also members of BIMCO as well as members of The Institute of Shipbrokers in London where they preach and practice the term “Our word, our bond”.

Fixture Notes:

There are however Owners and Charterers who engage in Charter Parties directly. Sometimes they tend to fix vessels on a “Fixture Note” which is a brief contract having just the major points of a Charter such as Freight (or Daily hire rate), Laycan, Loading and Discharging rates and Demurrage and Despatch rates. They avoid the use of lengthy charter parties.

COA:

And finally, we also have the existence of COAs or Contract of Affreightment, the main purpose being to “oblige a carrier to lift a fixed or determinable quantity of cargo of a specified type over a given period of time.” Usually, this contract is not restricted to one particular vessel, but operates as a series of voyage charters.

(Original by F R Chowdhury in July/ 2011 & revised by Capt. Ghulam Hussain in Dec/ 2017).

BOILER WATER TREATMENT

By Maklub Al Mostofa

Scale formation and corrosion are the main two factors that determine the efficiency of the internal parts and as well as lifetime of the boiler. Badly corroded and scaled boiler can fail within very short time.

SCALE FORMATION IN BOILER

Depending upon the sources boiler water contains various types of salts and impurities. Under operating conditions all the salts comes out of the water. These salts cause formation of scale inside the boiler. The more the water contains solids and salts the more the boiler is prone to scale formation.

Treatment:

Scale formation can be prevented in two ways.
1. External treatment:
– Use as pure water as possible.
– Proper feed water treatment.
– Keep the cascade tank clean. Maintain the cascade tank filter and feed pump filters cleaned.

2. Internal treatment:
– Carry out partial blow down of the boiler regularly and effectively.
– Regularly test the boiler water to determine the dissolved solids and salts.
– Chemical dosing should be done as per the test result to keep the boiler scale free.

Significance of regular partial blow down:
1. As the temperature rises the chloride comes out of solution that raises the boiler chloride level. Regular partial blow down from the bottom helps to maintain the chloride level.
2. Due to operating conditions the water may become acidic. Partial blow down of the water may reduce chemical dosing.
3. Remove sludge or mud from the boiler that precipitates at the bottom of the boiler.
4. Reduce the dissolved solid.
5. Reduce floating particles by scum blow down.
6. Reduce the water level in the boiler to prevent carry over or priming.

What is coagulant?

BOILER COAGULANT is a liquid sludge conditioner designed to prevent the formation of solid and sticky deposits in boilers.

How does it work:
boiler coagulant is a physical dispersant product that prevents the formation of large particles in liquid. It functions by keeping solids as small particles and prevents agglomerations from forming.
Boiler coagulant is primarily used in conjunction with hardness / phosphate control. The solids can be removed by the blow down as usual.
In addition boiler coagulant can help to remove small amounts of oil contamination if it arises, by blow down. Oil contamination must of course be stopped if it has arisen.

Boiler coagulant prevents the formation of adherent deposits and sludge in boilers and thereby reduces clean-downs.

Dosing Instructions
Normal dosage is 20ml daily/tone of boiler water capacity. Typically this equates to 0.1-0.3 liters/day. This is the recommended initial dose.
Boiler coagulant should be dosed directly to the boiler via the bypass pot feeder installed in the boiler feed water line.

Why the chloride level is always higher in the boiler than the condensate water in the cascade tank?
Answer: The water enters the boiler from the cascade tank will evaporate .Produced steam is very fine and will contain so chloride as it is heavier .So the chloride will remain in the water drum. As more feed water will enter the boiler the chlorides will be added .This process is continuous and if the chlorine id not blown down regularly it will go beyond limit though using distilled water.
The feed system is also prone to atmospheric contamination (sea environment is salty) at various points of the feed system.

HARD AND SOFT WATER:

Boiler feed water quality is most important factor that contribute the boiler efficiency. Poor control or treatment of the feed water could lead the boiler to be damaged within very short time.
Depending upon the purity boiler water be divided into two types
– Soft
– Hard

Hard water contains scale-forming impurities while soft water contains little or none.

Hardness is caused by the presence of the mineral salts of calcium and magnesium and it is these same minerals that encourage the formation of scale.

There are two common classifications of hardness:

 Alkaline hardness: it is also known as temporary hardness because the hardness is removed by boiling. Calcium and magnesium bicarbonates are responsible for alkaline hardness. The salts dissolve in water to form an alkaline solution. When heated up the salts decompose to release carbon dioxide and form soft scale or sludge.
.
Non-Alkaline Hardness Salts also known as permanent hardness salts are due to the presence of sulphates, chlorides, nitrates and silicates of calcium and magnesium. With the exception of silicates and the calcium sulphate, the permanent hardness salts are all very soluble in water and do not normally produce scale, but they are electrolytes and their presence, therefore, favours corrosion by galvanic action.
These salts precipitate out of solution as the temperature rises, and form hard scale, which is difficult to remove.
Silica can lead to hard scale and react with calcium and magnesium salts to form silicates which can severely resist heat transfer across the fire tubes and cause them to overheat.

What is dissolved oxygen?
Why it exists in boiler water?

Dissolved oxygen (DO) is the amount of oxygen (O2) dissolved in the water.

Oxygen enters the water at the surface of the water where exchange between the atmosphere and the water can take place.

The amount of dissolved oxygen that the water can hold depends on
– The temperature. DO reduce as the salinity increases.
– Salinity of the water. DO reduces as the temperature rises

How dissolved oxygen is removed where no mechanical de-aerators are used ?

The condenser is a heat exchanger which removes the latent heat from exhaust steam so that it condenses and can be pumped back into the boiler. This condensing should be achieved with the minimum of under-cooling, i.e. reduction of condensate temperature below the steam temperature. A condenser is also arranged so that gases and vapors from the condensing steam are removed
It is also done by chemical dosing.
Cascade tank also assists in removing oxygen as the temperature is maintained within 80-90 degree celciuous.

Why it dissolved oxygen is dangerous?

Boiler water ionizes into H+ and OH- ions. Dissimilarity in the ferrous metal forming the boiler surface will cause the surface to become partly positive and partly negative. The positive H+ ion attracted by negative cathodic area and by taking one electron it becomes H atom. While the negative OH- ion attracts positive anodic area and will produce ferrous hydroxide. If the oxygen is present it will react with ferrous hydroxide and corrode the boiler.
If the boiler water is properly alkalized and does not contain dissolves oxygen the H atoms will form a stable layer on the metal surface. In still water the ferrous hydroxide will remain insoluble and form a protective layer of magnetite in contact with the iron and no further corrosion will take place.

The main purpose of boiler and feed water treatment is to have a scale free and corrosion free boiler internals.
To prevent corrosion the boiler tubes needed to be passivated. Corrosion occurs when such passivated layer of magnetite becomes unstable or when chemicals are allowed to come between it and the base metal.

What is corrosion?

Oxidation: it is the chemical process by which metals gives up electrons.
Reduction: it is the gain of electrons in a chemical reaction. It is also known as redox. It is the opposite of oxidation.
Cathode: The cathode of a device is the terminal where current flows out..
Anode: An anode is the electrode in a polarized electrical device through which current flows in from an outside circuit.

IONS are the charged particles of substances. Ions are of two types
– Positive Ions
– Negative Ions

CHEMICAL COMPOSITION OF WATER:

pH elaboration is power of hydrogen. It is defined as the reciprocal logarithm of hydrogen ion concentration in water.

We know, water is the composition of hydrogen and oxygen. When it ionises splits into OH- & H+.
1liter water contains 10-14gm ions at 25 degree C. At neutral condition it contains 10-7gm H+& 10-7 gm OH- ions.
If OH- ion concentration increases it becomes alkaline.
If H+ ion concentration increases it becomes acidic :
The pH value is influenced by temperature.
pH value can be changed by chemical dosing.

Corrosion of boiler metal:

  • It is an electrochemical reaction of iron where corrosion occurs at cathode as the boiler metal oxidizes and dissolves.
  • This metal is extracted from the natural ore by reduction process in the refiner. This metal has natural tendency to go back to its natural state through oxidation and interaction with suitable environment. This natural tendency is the driving force of corrosion.
  • It is the general tendency of metals to be oxidized. Corrosion is a reduction/redox reaction.
  • Corrosion occurs at the anode, where metal oxidizes and dissolves.
  • At cathode, reduction takes place
  • Reaction at anode:  At anode Iron is oxidized to Fe++ , ferrous ion , Fe = Fe2+ + 2e¯

  • Reaction at cathode:    O2 gets reduced to OH- ions at cathode, Fe2++ ions are combining with OH- ions to form Fe(OH)2, ferrous hydroxide, Fe2+ + 2OH¯ = Fe(OH)2.

If the boiler water is properly alkalized and does not contain dissolves oxygen the H atoms will form a stable layer on the metal surface. In still water the ferrous hydroxide will create a protective layer of magnetite and no further corrosion will take place.

What is magnetite layer in boiler?

Magnetite is an iron oxide, [Fe3O4]. It deposits in the form of thin layer on boiler steel surface and passivate the surface and thus it resists the influence of water and contaminants to further react with the steel material.
Magnetite is formed on clean, pickled steel by two reactions:

1. Electro chemical reaction that takes place as follows:
3Fe (OH)2 = Fe3 O4 + H2 + 2H2O
The iron hydroxide is initially produced by reaction between iron and water. The reactions start around 100C and increase as the temperature increases.
2. Hot oxidizing reaction when magnetite is formed directly at temperatures 300 C or approximately at 30 bar boiler pressure. The reaction follows this route:
3Fe + 4H2O ( 300C+) = Fe3 O4 + 4H2

Types of corrosion:
a. Galvanic corrosion
b. Acidic corrosion
c. Caustic corrosion
d. Hydrogen corrosion
e. Stress Corrosion
f. Corrosion fatigue
g. Pitting corrosion

Galvanic corrosion:

We all know it needs two dissimilar materials to create a galvanic cell. Boiler tube material is steel. Then how the galvanic cell forms?
Boiler condenser tubes are made of copper and boiler tube material is made of steel. Copper may react with oxygen and may be carried as copper oxides inside the boiler. This two dissimilar materials are mainly responsible for galvanic corrosion.
Galvanic cells also form due to temperature difference, scales, salts, bacteria, oil contamination, conductivity, scratches in the material etc.

Acidic corrosion:

Acidic water has an excess of hydrogen ions which leads to hydrogen evolution. The Protective film of hydrogen gas on the cathodic surface breaks down as the hydrogen combines and bubbles off as diatomic hydrogen gas.
Acid corrosion may also occur due to heavy salt water contamination or by acids leaching into the system from demineralisation regeneration.

Oxygen: We know at cathode, Fe2++ ions are combining with OH- ions to form Fe(OH)2, ferrous hydroxide, Fe2+ + 2OH¯ = Fe(OH)2
If oxygen is present it will react with ferrous metal surface to form red iron oxide F2O3 result in pitting corrosion
The ferrous hydroxide then combines with oxygen and water to produce ferric hydroxide, Fe (OH) 3, 4 Fe (OH) 2 + O2 + 2 H2O –> 4 Fe (OH)3.
Ferric hydroxide dehydrates to rust,
F2O3, Fe (OH)3 ⇌ FeO(OH) + H2O . FeO (OH) ⇌ F2O3 + H2O.
Rust consists of hydrated iron (III) oxide, F2O3·nH2O and iron ( III) oxide – hydroxide ,(FeO(OH), Fe(OH)3).

CO2: React with water to form carbonic acid, which reduce the pH of the water and accelerate corrosion

Ammonia: Attack the copper base alloy in the present of oxygen

Hydrogen attack:

Hydrogen irons are generated by concentration of acid under a hard dense deposit. It can penetrate the grain boundary of tube metal and react with carbon and produces methane gas. This carbon loss weakens the tube metal and methane gas exerts a pressure which separates the grains of tube.
Hydrogen attack can also occur when hydrogen is released by caustic corrosion.

Caustic corrosion:

Caustic: Caustic is the other form of solid alkali added to the boiler
Caustic corrosion (gouging) occurs when caustic is concentrated and dissolves the protective magnetite (Fe3O4) layer.
This form of attack can take place at high pressures due to excessive concentrations of sodium hydroxide. The sodium hydroxide forms local concentrations nearly coming out of solution and forming thin film close to the heating surface. This breaks down the magnetite layer and then reacts with the steel to produce a soluble compound which then deposits on the surface in the form of a layer of loose porous oxide.

Corrosion fatigue:

While high temperature surface suffers from poor circulation of water and the surface is under stress it may form a series of f line cracks in the wall. Corrosive conditions aggravate the condition.

Stress Corrosion:

It needs two factors to act together which leads to stress corrosion.
– Stress
– Corrosive environment
Due to corrosive action protective layer may break down and form a local weak point. If this area is subjected to heavy alternating stress fatigue crack may result. The bare metal will then be subjected to further corrosive action causing the process to continue. Mechanical stress of boiler parts may be due to mal-operation of the boiler, raising steam too rapidly from cold, missing or poorly connected internal feed pipes, fluctuating feed temperature and steaming conditions.

Pitting corrosion:

Corrosion is mainly a local corrosion. It needs relatively a large cathodic area and a small anodic area. Hence the intensity of attack at the anode is high. Large area differences could be caused by mill scale, oxide films, acid pockets of water, scale from salts, pores or crevices, oils, gases and ingress of metals into the boiler. Corrosion rate increases with temperature, hence where metal surfaces are hottest failure may take place earlier.

What is caustic hide out?

Caustic is the other form of alkali added to the boiler
As the name implies the caustic present in the boiler water remains untraced during water test. Hence it is termed as caustic hide out.
Due to the rapid evaporation the sodium hydroxide forms local concentrations that come out of solution and forming thin film close to the heating surface.
However if the evaporation rate is reduced the hydroxide is released back into normal circulation and the alkalinity is apparently restored. This phenomenon is referred to a caustic hideout.
This breaks down the magnetite layer and then reacts with the steel to produce a soluble compound which then deposits on the surface in the form of a layer of loose porous oxide.

Q. When a steam boiler water tube is started leaking,
(a) How do you know?
(b) How will you check the leaking source?
(c) What are the remedies available?
(d) How will you repair to proceeds the rest of journey?

How to know:
1. As steam consumption is more feed pump will be continuous running.
2. Excessive feed water consumption from cascade tank or feed water tank.
3. If the large amount of leakage, boiler water level will be low, steam pressure will be drop and continuous firing of boiler.
4. Some water comes out from furnace cover.
5. White smoke emitting from boiler uptake.

The possible sources of the entry of water may be considered at
1. The leakage tubes.
2. Distorted furnace crown plate.
3. Furnace shell plate opposite of the burner opening due flame impingement.
4. The lower section plate of furnace due damage brick-works.

The possible causes of leakage:
1. External wastage: due to waterside corrosion and pitting. Corrosion and pitting may occur due to
– Poor quality feed water
– Ineffective treatment

2. Uneven thermal expansion: this can happen between tube and tube plate due to local overheating. Overheating could be due to low water condition, heavy scale, oily deposits or forcing of the boiler.
3. Deformation of tube plate: Under pressure would have the overheating effect that tube fail at the tube end of the tube plate.
Check procedure:

For water tube boiler (Z boiler):

1. Stop the firing
– open up the combustion chamber,
– Fill up the boiler water level to full.
– leakage can seen easily be seen & identify the individually boiler water tube

For smoke tube boiler:
– Stop the firing
– open the smoke side drain valve,
– If there is any leakage water will come out.

Once tube leakage is confirmed steps will be taken to identify the leaking tube.

– open up the fire side cover
– fill up the boiler water level until all smoke tubes are flooded,
– We can easily to check which one is leaking ligaments.

Remedies
Repairing could be carried out by inserting tube stopper or new tube renewal.
The defective expanded tube is found originally expanded and bell-mouthed at the tube ends. The first step is cropping at the ends about 50mm from the tube plate and chisel off. The remaining pieces are removed by chiseling and knocking out after heating and cooling to achieve shrinkage.
Then the tube holes to be cleaned and polished before dye penetrant test for any cracks. Minor blemishes at the tube hole are made good with light rolling by an expander.
The usual diametrical clearance between the tube and tube hole being about 1.5mm, this must be taken into account while renewal of this tube. The tube ends of the new tube are cleaned thoroughly and carefully roller expanded into the hole in the tube plate.
When the new tube is placed in the tube hole, they must project through the tube plate by at least 6mm. The bell mouthing is to be 1mm for every 25mm of outside diameter plus 1.5mm.

SCAVENGING AND TURBOCHARGING (QUESTIONS & ANSWERS)

By Maklub Al Mostofa

Q. What is scavenging? Name the types of scavenge used for large two stroke engine. Describe the advantage of Uniflow scavenging.

SCAVENGING:
It is the removal of residual exhaust gas and its replenishment with fresh air in an internal combustion of the engine. The fresh air intake and exhaust gas expel operation are not simultaneous fully but some degrees of overlap period are provided for better efficiency.
There are 3 types of scavenging process.
1. Loop scavenging
2. Cross scavenging
3. Uniflow scavenging

Loop scavenging:
In this type of scavenging air passes over the piston crown and rises to form a loop. Ports are cut in the cylinder liner wall for this operation. The scavenge ports and exhaust ports are in the same side of the liner.

Image credit: Introduction To Marine Engineering by D A TAYLOR

Cross scavenge:
In this type of scavenging the scavenge air is directed upwards and expelled from the opposite side of the liner. Scavenge and exhaust Ports are cut in the cylinder liner wall for this operation. The scavenge ports and exhaust ports are in opposite side of each other.

Image credit: Introduction To Marine Engineering by DA TAYLOR

Uniflow scavenging:
In this type of scavenging scavenge air enters through ports near the bottom of the liner then travels straight up the liner and forcing the exhaust gas to expel from the top through valve arrangements. This gives maximum efficiency of scavenging.


Image credit: Introduction To Marine Engineering by D A TAYLOR

Advantages of Uniflow scavenging:
• Highest efficiency of scavenging and Very little amount of exhaust and scavenge intermixing.
• Provides higher degrees of overlapping period hence increasing efficiency of the engine.
• Allow simplicity of liner as fewer ports are cut.
• More liner cooling is achieved/Thermal stresses are less compared to other method of scavenging.
• Avoid long piston skirt.
• Make satisfactory & economical of cylinder lubrication/ Cylinder L.O. consumption is reduced.
• Efficient design for long stroke engine.

“Pulse” system:


Image credit: MARINEDIESELS.UK.COM

 The Pulse system takes advantage of the higher pressures and temperatures of the exhaust gases during Blow—down period and with rapidly opening of exhaust valves or ports.
 The gases leave the cylinder at high velocity as pressure energy is effectively converted into kinetic energy to create a pressure wave or pulse in the exhaust pipe.
 The pipe so constructed in small diameter is quickly pressurised and boosted up to form a pressure pulse.
 The pulsating pressure waves reach up to the turbine nozzles and further expansion takes place.
 The pressure in the exhaust pipe before the turbine shows a cyclic variation as is evident from the pressure crank angle diagram.

Advantages of pulse system:
1) High available energy at turbine.
2) Good performance at low speed & part load.
3) Good turbocharger acceleration.
4) Highly responsive to any changing load due to small volume of exhaust ducting
5) Required no scavenge assistance at any changing load

Disadvantages:
1. The exhaust grouping is complicated.
2. Different sizes of exhaust pipes are needed for spare.
3. Exhaust tuning and grouping requires special attention to avoid back flow and incorrect tuning could seriously affect the engine performance.

Constant Pressure System:

Image credit: MARINEDIESELS.UK.COM

 In the constant-pressure system, exhaust gases from all cylinders pass into a common large diameter exhaust manifold.
 This is of sufficient capacity so that the intermittent exhaust from the different cylinders does not cause pressure fluctuations.
 Because of the fairly constant gas pressure and temperature at the turbine inlet; it operates at about its optimum efficiency.
 This system is most suitable for high output engines, and there is no need to group the cylinder exhausts into multiples of three.
 A major disadvantage of the constant-pressure system is that when running at reduced speed and especially when starting up, the pressure energy available at the turbine inlet is insufficient to drive it fast enough to supply the quantity of air at the scavenging pressure necessary for efficient scavenging and combustion.
 Therefore, it is necessary to be made an additional source of air compression, such as reciprocating pump or turbo blower.

Turbocharger Arrangement in Constant Pressure System:

• No exhaust grouping required and pipe distribution is simple.
• Exhaust gases enter into large common manifold and then to turbine
• Firing order not considered

Advantages:
1. Good performance in high load.
2. More suitable for high output engine.
3. There is no need to group the cylinders exhaust into multiple of three.
4. High turbine efficiency due to steady flow of exhaust.
5. Reduction in SFOC (Specific Fuel Oil Consumption)

Disadvantages:
1. When running at reduced speed and starting up low available energy at turbine. Thus it supplies inadequately air quantity of the scavenge pressure necessary for efficient scavenging and combustion.
2. It requires Auxiliary Blowers.
3. Poor response in changing load.

Turbocharger Surging:

• It is the aerodynamic phenomena which produces a back flow of air from discharge to suction side (impeller and diffuser) when the discharge volute pressure exceeds the pressure build up in the suction side and it causes heavy noise and vibration of turbocharger.
Causes of Turbocharger Surging:

1. Suddenly load change by heavy sea
2. Scavenge space fire
3. Exhaust trunk fire
4. Poor power balance
5. Dirty nozzle and blades
6. Individual cylinder misfire
7. Chocked scavenge /exhaust ports
8. Incorrect matching of turbocharger to engine.
9. Poor scavenging or leaky exhaust valve

Advantages of Inter Cooling the Charged Air:
• Reduce scavenge air temperature
• increase the density of air delivered to the cylinders
• Increasing the power output delivered by the engine.
• Cooled scavenge air reduces cylinder and exhaust gas temperature at a given power level.
• Maintain temperatures within the acceptable limits.

Types of Turbocharger Lube Oil System
There are two methods of lubrication:
1. Own sump
2. External lube oil supply system

Types of Turbocharger Bearings

Q. Describe the type of T/C bearings. Discuss their strength & weakness.

Ans: There are two types of T/C bearings:

1. Sleeve Type.
2. Ball or roller type.

Ball type bearing (rolling type):
The ball and roller bearings are mounted in resilient mountings incorporating spring damping to prevent damage due to vibration. These bearings have their own integral oil pumps and oil supply, and have a limited life.

Advantages of ball or roller type bearing:
• Less friction losses.
• Minimal lubrication
• Greater alignment accuracy.

Disadvantages of ball or roller type bearing:
• More expensive.
• Limited life time
• Need higher grade lubrication.
• More susceptible to vibration and fatigue

Sleeve type bearings:
• Sleeve type bearings are lubricated by external L.O supply system. This is achieved either by
– Gravity from independent header tank situated about six meters above the bearings to ensure that LO pressure never drops below 1.6 bar. Or by
– A main L.O pump leads to the bearings with a separate L.O pipe line. It has also gravity tank in case of failure of L.O supply. The system incorporates fine filters to avoid impurities and foreign particles.

Advantages of sleeve type bearing:
• Load carrying capacity is more.
• It can run at higher temperature.
• Better inlet flow.
• Shorter rotor length
• Higher efficiency under full load condition.
• Time between overhauling is more than the other types of bearings.

Disadvantages of sleeve type bearing:
• At low speed/load create high friction.

Function of Labyrinth Seals:
• Labyrinth seals are of specially designed metallic fin type seals that separate the bearings from the blower and turbine.
• These seals are sealed by air supplied from the compressor volute casing is led into a space to prevent oil entering the blower and to prevent contamination of the oil by the exhaust gas.

Q. What is exhaust tuning?
• Ans: Exhaust tuning is the arrangement of exhaust pipe lay out with suitable length & proper v/v timing to exhaust into the same pipe without affecting the engine performance.

Q. How the exhaust of one cylinder is prevented from interfering the scavenging of another in the pulse system?

Answer: In pulse system, the exhaust of one cylinder is prevented from interfering the scavenging of another as follows.
– Exhaust system is tuned so that the manifold pressure pulsation is not reflected back to engine as backpressure.
– As the exhaust valve of a diesel engine opens, the gases in the cylinder rapidly expand and gain velocity and kinetic energy as they pass into the exhaust pipe.
– As the exhaust gas travels through the manifold it causes partial vacuum behind it.
– The cylinders are so connected to a common exhaust pipe so that the exhaust valve of the second cylinder is opened when the exhaust from the first cylinder has created a vacuum in the pipe
– Exhaust from the second cylinder will be discharged more easily.
– Thus the tuned exhaust system with the exhaust pipes a suitable length and arranging for two or three cylinder with suitable exhaust valve timing prevented from interfering the others.

Q. State the indication of scavenges fire.

Ans: Indication of scavenge fire:
• High exhaust temperature of corresponding unit.
• High local temperature in scavenge trunk.
• Black smoke in exhaust gas.
• Burning smell
• Surging of T/C.
• Flame, spark or smoke emitted from the scavenge drains.
• Loss in power, irregular and fluctuating rpm of engine.

Q. Describe the causes & prevention of scavenge trunk fire?

Ans: Causes of scavenge fire:
• Accumulation of unburned fuel or cylinder L.O. in scavenge trunk.
• Blow past of the engine due to over load or bad piston rings..
• Bad combustion due to bad fuel management.
• Faulty injector and fuel pump timing.
• Excessive cylinder lubrication.
Prevention of scavenge fire:
• Regular draining, cleaning and monitoring of the scavenge space.
• Correct rate of cylinder lubrication.
• Proper maintenance & correct adjustments of piston rings, cylinder liner and fuel injection equipments.
• Ensure balanced engine.
• Safety devices such as electrical temperature sensing, pressure relief valves should be fitted in the scavenge trunk.

Q. How scavenge fire can be avoided? What are the safety devices incorporated in an engine for scavenge fire.

Ans: Step to avoid scavenge fire:
• Proper maintenance of the fuel injection equipments, piston rings as per maker instruction.
• Not to over load the engine.
• Periodically cleaning and inspection of scavenge trunk.
• Regular draining of scavenge trunk.
• Monitor the under piston scavenge space temperature

Safety devices for scavenge trunk:
• Scavenge trunk relief valve.
• High temperature sensing device with alarm.
• Fixed fire extinguishing system.
• Sight glass on scavenge drain line.
• Non-return valve.

Q. Describe the action to be taken in case of scavenge fire.

Action to be taken:
• Activate fire alarm.
• Inform bride & chief engineer.
• Stop the engine but L.O. pump keep on running.
• Engage turning gear & rotate the engine.
• Apply fire extinguishing medium to scavenge trunk.
• Arrange boundary cooling.

For more details, you can visit the the link:                                  http://marinestudy.net/diesel-engine-scavenge-fire/

Q. With reference to large T/C state-
a) How air & gas tightness between rotor & casing achieved?
b) Explain how the gas can raise the pressure of air higher than its own?
c) What is the purpose of nozzle ring?

Ans: a) Air & gas tightness between rotor & casing achieved by allowing some of the air from compressor outlet through a labyrinth arrangement which act as a seal.
b) The gas can raise the pressure of air higher than its own because of T/C.
• The inducer guides the air flow smoothly into the eye of impeller which throws the air outwardly increasing velocity due to centrifugal force at high rotational speed.
• The diffuser reduces velocity by converting kinetic energy into pressure energy and leads the air to the volute casing.
• The volute casing further decreases the velocity and increases the air pressure.

c) Purpose of nozzle ring:
• Expand the exhaust gas and direct exhaust gas to turbine blade.
• Convert the pressure energy of gas to kinetic energy giving a high velocity.

Q. Purpose of inducer.
Ans: .
• The purpose of inducer is to guide the air smoothly into the eye of the impeller.
• It also takes shock of the incoming air therefore supplying smooth air into the impeller.
Function of Diffuser in turbochargers?
• To direct the air smoothly into volute casing
• Convert kinetic energy to pressure energy.
What is K value in turbochargers?
• It is the distance between the rotor shaft end and the flange of bearing cover measured by blower side.
• It is critical clearance necessary to avoid contact rotating impeller and stationary blower casing cover in case of thrust bearing worn out.

Q. With reference to T/C give reasons for corrosion on the: a) gas side b) air side c) water side.

Ans: Reasons for corrosion on gas side:
• Poor combustion and carryover of oil causes carbon build up in nozzles and blades. It prevents proper heat exchange.
• Oxide of sulphur from combustion may cause acidic corrosion under light load with low exhaust temperature.
• Vanadium & sodium ash from fuel combustion may deposit & causes local burning.
• Deposit of calcium sulphate cylinder L.O. may causes corrosion.
Reasons for corrosion on air side:
• Oil vapour & Dust from engine room may sucked by the compressor & causes corrosion on air side.
• Salty moisture which is present in the air at sea sucked by the compressor & causes corrosion.
Reasons for corrosion on water side:
• Water side may be corroded by electro- chemical if the pH value of water is low i.e. water is acidic.
• If there is inadequate protection against sea water corrosion.
• Improper cleaning schedule or PMS.

Q. With reference to the T/C state-
a) Why turbine blades are loosely attach to the rotor?
b) How axial movement of the turbine blade is prevented?
c) How blade vibration is dampened over a wide range of speed?
d) What is the purpose of sealing air?

Ans:
a) The root is usually a slack fit to allow for differential expansion of the rotor and blade and to assist damping vibration. Blade roots are of fir tree shape which gives positive fixing and minimum stress concentration at the conjunction of root and blade.
b) Axial movement of the turbine is prevented by fixing the locking strip.
– In case of ball & roller bearing turbocharger axial thrust is balanced by lamina damping spring assemblies in bearing housing.
– In case of sleeve type bearing turbocharger axial thrust is balanced by sealing air which is fed to the chamber behind the turbine disc from compressor outlet at sufficient r.p.m. of rotor.
– But at start up, shut down & very low speed axial thrust is taken by thrust bearing.
c)
d) Blade vibration is dampened over a wide range of speed by binding the blade with a lacing wire. The wire passes through holes in the blades and damps the vibration due to friction between the wire and blade. It is not fixed to each individual blade.

IMAGE CREDIT: MARINEDIESELS.UK.COM

e) Purpose of sealing air:
• Seal the labyrinth gland to protect L.O. contamination by exhaust gas at turbine side.
• Seal the labyrinth gland to protect L.O. & air mixture at blower side.
• Cool the rotor shaft & turbine disc.
• Oppose the axial thrust towards compressor.

Q. With reference to the T/C state- Cooling water casing got holed, how to run T.C?

Internal water leakage:
– Stop the engine.
– Stop water supply
– Arrange compressed air supply as coolant.
– Attention must be paid to the operating temperatures especially for the turbine end bearing.

Q. Advantage of charge air cooler.
Ans:
• Increased density of air ( allow a greater mass of air to be compressed)
• Increases scavenge efficiency.
• Increases output power.
• Increases fuel burning capacity.
• Engine is maintained at safe working temperature.
• Reduced thermal stress on piston rings, piston & liner.

Q. How will you know turbocharger air filter chocked?

Ans: Filter condition can be assessed by the following parameters and symptoms:
• Greater differential pressure at turbo charger filter.
• Reduced engine power.
• Black smoke from the funnel
• Less Scavenge pressure
How will you run engine in case of turbocharger failure?
• Engine to be stopped.
• Rotor to be blocked
• Exhaust gas to be by-passed the turbocharger
• Run engine with reduced speed with remaining turbocharger
• Use Auxiliary Blower
• Maintain all temperature and pressure of fuel, cooling water and lubrication within limit

Q: During normal engine operation a turbocharger rapidly loses speed and the speed reduction is accompanied by appreciable noise.
(a)State with reasons the possible causes.

The two factors of loud noise and rapid speed reduction indicates that rotational
friction has dramatically increased, or the rotor is in contact with the stator, which
could be due to
◊Bearing failure: Bearing failure will affect the rotor clearances, causing the rotor to contact the stator. Bearing may fail due to
– Lack of lubrication
– Dirty lubricant
– Lack of cooling
– Excess vibration
– Failure due to fouling
– Failure of the resilient mounting
– Over running hour.
– Faulty sealing system.
◊Mechanical damage to the rotor: If any component from the combustion chamber is admitted to the exhaust side of the rotor, the rotor will be imbalanced and may leading to possible bearing failure.
◊Failure of the water coolant casing: This will admit water to the gas inlet and cause a reduction in the rotor speed

b. State with reasons the factors which may limit engine operating speed with the turbocharger out of operation

Ans:

The exact power limit with a defective turbocharger will depend upon the actual configuration of the system and how many turbochargers remain in operation
The following factors need to be considered when operating the engine:
◊Exhaust temperatures: The actual operating conditions should be taken into consideration and engine manual would be consulted as to the maximum limit
◊Exhaust smoke levels: Exhaust color should be monitored. Allowance should be made for the change of rate acceleration to prevent excessive thermal load.
◊Maximum engine power: This will be limited due to the factors stated above, and this will probably be approximately 50% power with the loss of one of the two turbochargers.
Hence the engine power would be reduced in consideration with all the above factors.

With reference to turbo-chargers:
a) state how the in-service performance checks are undertaken for EACH of the
Following:
i) the gas side
ii) the compressor
iii) the suction filter
iv) The after cooler
b) State with reasons the action require to maintain satisfactory performance of
i) The turbine
ii) The compressor
b) Should in-service vibration be experienced state with reasons the possible causes?

GAS SIDE: The main monitoring data is the temperature differential across the T/C for a given turbocharger speed. It gives an indication of energy converted by the gas side, i.e: nozzle ring and blade. The fall off performance of these components would be mainly due to fouling.

COMPRESOR SIDE: The compressor performance would be reduced by fouling of the compressor wheel and diffuser. This fouling would also cause the scavenge air pressure to fall, whilst the
T/C was maintaining a stable speed and all other parameters were normal. Hence the delivery pressure of the compressor would be monitored.

SUCTION FILTER: The suction filter performance can be checked by the followings:
– Scavenge air pressure
– Pressure drop across the filter. A manometer fitted across the filter will show an increase in differential pressure.

AFTER COOLER:
The after cooler performance would reduce when fouling is present.
– If the fouling is at the air side this would be monitored by measuring the air pressure drop across the cooler.
– If the fouling is at the water side this would be monitored by the reduction in temperature difference between the cooling water inlet and outlet.

The performance of the turbine is maintained by:

– The fuel combustion should be kept to an optimum condition.
– The cylinder oil doses should be avoided.
– Regular in-service cleaning, The in-service cleaning can be carried out using either dry cleaning involving dry particle cleaning, and/or water washing of the turbocharger using warm water and air blast .
– Manual cleaning of the turbocharger on a yearly operational running hour routine.

The performance of the compressor is maintained by:
– Regular in-service cleaning, supplemented by manual cleaning of the compressor and diffuser on a yearly operational running hour routine.
– The in-service cleaning can be carried out using a small quantity of warm water injected into the turbocharger suction housing at full T/C speed. This cleaning can be carried out twice weekly.
– The air drawn into the compressor should be as clean as possible. The air filter should be maintained in good condition.

The T/C can vibrate due to the following causes:

– Rotor imbalance following inadequate in-service cleaning.
– Vibration can be caused by the blade failure due to corrosion, fatigue, failure of a portion of lacing wire.
– Rotor imbalance due to failure of the rotor support bearings.
– Rotor imbalance due to rotor damage from an object displaced from the cylinder, such as a broken piston ring or exhaust valve.
– Surging of the turbocharger, when the unit is operated close to the surge line possibly due to a fouled hull.

– Vibration transmitted to the turbocharger unit from an adjacent machinery unit.

Following a recent turbocharger overhaul it is observed that the scavenge air pressure is lower than it was previously and the engine power output is also reduced.
a. State, with reasons, the possible causes of the problem.
b. State, with reasons, what engine operational information should be gathered in order to enable the possible cause of the problem to be detected.
c. Explain how the defect may be rectified.
d. State the instructions which should be issued with respect to future turbocharger overhauls in order to prevent similar incidents.

Answer:

a.
A turbocharger overhaul consists of removing the rotor and nozzle ring for inspection and cleaning, renewing the bearings where necessary, inspection of the labyrinth glands, cooling water spaces and gas inlet protection grid.
Causes of low scavenge pressure are:
– Dirty air filter. Overlooked cleaning the air filter before refitting.
– Scavenge dump valves left open.
– Damage to turbine blades. This could have occurred when removing refitting rotor. The efficiency of the turbine will be reduced if the blade profile is damaged. May also cause vibration.
– Damaged impeller; again while removing or refitting. See above.
– Defective or incorrectly fitted bearings allowing rotor to rub against casing labyrinth glands may be damaged as a result.
– Foreign bodies in protection grid, nozzle ring, turbine blades, compressor or diffuser. Compressor axial clearances incorrect due to badly fitted bearing; allowing air to leak back from discharge to suction. May also cause back of compressor wheel to rub against casing.
– Waste gate or a charge air by pass valve, may be jammed open or not operating correctly (if fitted)

b. Operational information to be gathered:
– Turbocharger speed: The faster the turbocharger revolutions, the greater mass flow of air produced, and the higher the scavenge pressure. Slow turbocharger rpm could be an indication of all of the above faults.
– Vibration (and noise): Vibration can indicate damaged unbalanced rotor; noise indicates rotor in contact with casing.
– Exhaust gas inlet temperature to turbo-charger: A higher than normal temperature (along with higher exhaust valve temperatures)are an indication of a high exhaust gas back pressure could be caused by choked nozzle ring.
– Exhaust gas temperature difference across turbine: A smaller than normal differential will indicate that the exchange in energy is not taking place across the turbine.
– Pressure drop across air inlet filter.
-Temperature differential across air cooler water inlet and outlet.
– Surging of the turbocharger
c.
If the T/C is vibrating or unusually noisy:
– Engine must be stopped and the cause investigated. This will entail removal of the rotor. Check compressor wheel, shaft, and labyrinth, turbine wheel for signs of damage or rubbing. Check casing and nozzle ring for damage. If damage has occurred then it must be rectified before the rotor is rebalanced and refitted with the correct bearings.
If there is no vibration or noise:
– Check dump valves, bypass and waste gate if fitted.
– Check that the air filter is clean.
– clean the air cooler on the air side.
If none of these are successful, then it may be necessary to open up the turbo-charger and check that it has been assembled correctly with correct axial clearances and that there are no blockages in the nozzle ring or protection grid.

d.
The overhaul of the turbocharger should be overseen senior member of the engineering staff as appointed by the Chief Engineer.
– Only chemicals recommended by the manufacturer are to be used at the recommended strengths.
– After cleaning the turbine rotor and compressor wheels are to be examined closely for any sign of damage before re-assembly.
– New bearings to be fitted if the running hours are within 20% of the recommended maximum hours for the bearing.
– Only manufacturers spares, sealed in tins are to be used.
– Axial clearances must be checked and recorded after comparison with the original clearances
– Ensure that no gloves, rags, tools etc are left in the casing or exhaust pipes before boxing up, and that the protection grids are clean and in position.
– The air filters and air cooler is to be cleaned.
– Bypass valve and waste gates are to be checked for correct operation on completion of overhaul.

Turbocharger vibration:
Sudden vibration:
– Sudden imbalance due to blade damage
– Sudden imbalance due to partial dirt removal.
– Breakage of damping wires
– Breakage of resilient mounting.
– Bearing failure
– Poor cylinder combustion.
– Damaged support
– External excitation

Remedial action:

– Regular and effective in service cleaning.
– Effective LO management.
– Regular inspection of bolts and casing.
– Maintain optimum cylinder combustion condition.
– Protection grid condition

Gradual vibration:
– Ineffective in service cleaning.
– Gradual fouling
– Slackening of bolts
– Deterioration of resilient mounts for bearings.
– Ineffective PMS.
Remedial action:
– Maintain PMS
– Effective Water/solid wash.
– Regular bearing exchange
– Regular inspection and maintenance of the supports.

Q: State the Methods of operating with defective turbocharger.
Methods of running the engine with defective turbocharger depend upon design consideration and the repair facility.

Answer:

Bypass arrangement:

Some design provides a different path for the exhaust gas to pass to the uptake.
Engines with exhaust by-pass
1. Stop the engine.
2. Lock the turbocharger rotor.
3. Remove the blanking plate from the exhaust by-pass pipe.
4. Remove the compensator between the compressor outlet and the scavenge air duct. This reduces the suction resistance.
5. Run engine with reduced load.

Engines without exhaust by-pass:

This system allows the damaged rotor to be taken out of the engine. This may also allow repair work of the rotor is possible.
1. Stop the engine.
2. Remove the rotor and nozzle ring of the turbocharger.
3. Insert blanking plates.
4. Remove the compensator between the compressor outlet and the scavenge air duct. This reduces the suction resistance.
5. Cooling should be maintained for the turbine casing if possible.
6. Run engine with reduced load.

Engine with locking the rotor:
1. Stop the engine.
2. Lock the rotor of the defective turbocharger.
3. Rather than completely blanking off the compressor an orifice plate is fitted to allow controlled amount of cooling air to pass to prevent overheating of the rotor due to conduction
4. Cooling should be maintained for the turbine casing if possible.
5. LO supply to stop.
6. Run engine with reduced load.

Q. Describe how the following conditions are caused and dealt with
• Gradually decreasing in scavenges air pressure.
• Suddenly increasing in scavenges pressure.
• Scavenge air temperature at consistently above normal.

(a)Scavenging air pressure drops in spite of the normal speed of the turbocharger means that resistance has increased in the passage between air inlet and the scavenge air valves.
• Problem with the turbocharger
• Negative pressure set up inside scavenge trunk.
• Air suction filters fouling.
• Faulty scavenge air non-return valve.
• Charge air cooler fouling.
• Turbocharger deceleration.
• Scavenge fire.
• One of the cylinder units misfiring.
• Fouling exhaust system.
• Scavenge manifold leakage and scavenge drain valve open.
• Engine room pressure is negative due to bad weather.

(b) The scavenge air pressure may be increased suddenly because of the following facts:
• Adverse weather and strong wind.
• Overloading of engine.
• Faulty exhaust booster system.
• Auxiliary blower cut in.
• Just after water washing.

(c) The scavenging air temperature may be rising due to the following conditions:
• Fouling of charge air cooler.
• High engine room ambient temperature.
• Faulty cooling water control bypass system.
• Engine overload.
• Scavenge fire.
• Piston blow-past.

Remedies
So as to avoid these conditions already mentioned above, to carry out the following measures:-
• Charged air cooler is cleaned when the pressure differential exceeds the max limit, by reading the differential pressure at manometer fitted at charged air cooler for airside cleaning.
• Turbocharger blower side air filter is cleaned by checking the pressure different shown at “U” tube manometer attached at Blower side air filter housing.
• Charge air cooler’s seawater is cleaned by checking the cooling S.W inlet and outlet temperature difference.

REFERENCES:
DIESEL ENGINES BY A.J WHARTON
MARINEDIESELS.UK.COM
REEDS MOTOR ENGINEERING KNOWLEDGE
INRODUCTION TO MARINE ENGINEERING BY D A TAYLOR

OIL RECORD BOOK (QUESTIONS & ANSWERS)

By Maklub Al Mostofa

QUESTIONS:

  • How to put entry in ORB?
  • What is action in case of wrong entry?
  • How many people fill up and sign it?
  • What is your action if an entry is missed?
  • What is your action if you make any mistake?

 ANSWER:                               

      • This guidance only includes sections C to I.
      • Operations should be recorded in chronological order as they have been executed on board.
      • Dates should be entered in dd/mm/yyyy format, e.g. 16-MAR-2009.
      • Incineration or landing ashore of oily garbage and used filters should be recorded in the Garbage Record Book only.
      • All Entries are to be made and signed by the officer or officers in charge of the operations concerned and each completed page shall be signed by the master of the ship.
      • Do not leave any full lines empty between successive entries.

     

    • If a wrong entry has been recorded in the Oil Record Book (ORB), it should immediately be struck through with a single line in such a way that the wrong entry is still legible. The wrong entry should be signed and dated, with the new corrected entry following.
    • Tank nomenclature should be recorded as per the format noted within the International Oil Pollution Prevention Certificate (IOPPC).
    • Recording of quantities retained in bilge water holding tanks listed under the IOPPC (section 3.3) is voluntary and not required by the Convention.
    • The recording of general maintenance of items pertaining to the OWS remains voluntary and is not required to be recorded in the ORB.

    SOURCE: MEPC1/CIRC.736.REV.2

    QUESTIONS:

    1. What are the weekly entries to be made in ORB part1?
    2. Difference between code D and code E?
    3. What you will entry in case of oil filtering equipment failure?
    4. How you will entry bunker operation? What is the unit of recording?
    5. What are the additional entries?

    ANSWER:

    • Usage of code C.11: Collection of oil residues (sludge).
    • Item No 11.1 identity of tank(s)
    •  Item No 11.2capacity of tank(s) in m3,
    • Item No 11.3 Total quantity of retention in m3.
    • Item No 11.4 Quantity of residue collected by manual operation in m3.

    (Operator initiated manual collections where oil residue (sludge) is transferred into the oil residue (sludge) holding tank(s).)

    Example #1
    Weekly inventory of oil residues (sludge) tanks (tank listed in the Supplement to the IOPPC)

    Example #2 :
    Recording of oil residue (sludge) collected by manual operation in oil residue (sludge) tank- Note: Operator initiated manual collection where oil residue (sludge) is transferred (transfer with a pump) into the oil residue (sludge) tank(s). Examples of such operations could be:

    1. Collection of oil residue (sludge) from fuel oil separator drain tanks.
    2. Collection of oil residue (sludge) by draining engine sump tanks.
    3. Adding fuel oil to an oil residue (sludge) tank (all content of a sludge tank is considered sludge).
    4. Collection of sludge from bilge water holding tanks – in this case a disposal entry for bilge water is also needed.

    Usage of code C.12: Disposal or Transfer of oil residues (sludge)

    • Item No 12.1 to reception facilities (identify port)
    • Item No 12.2 to another (other) tank(s) (indicate tank(s) and the total content of tank(s));
    • Item No 12.3 incinerated (indicates total time of operation with time of start and stop);
    • Item No 12.4 other method (state which).

    Example #3:
    Disposal of oil residue (sludge) via shore connection
    Note: Ships’ masters should obtain from the operator of the reception facilities, which includes barges and tank trucks, a receipt or certificate detailing the quantity of oil residue (sludge) transferred, together with the time and date of the transfer. This receipt or certificate, if attached to the Oil Record Book Part I, may aid the master of the ship in proving that his ship was not involved in an alleged pollution incident. The receipt or certificate should be kept together with the Oil Record Book Part I.

    Example #4:
    Draining of water (disposal) from an oil residue (sludge) tank listed under item 3.1 in the Supplement to the IOPPC, to a bilge water holding tank listed under item 3.3 in the Supplement to the IOPPC :

    Note: Collection of bilge water need not to be accounted for, so only one entry is required. Capacity of sludge tanks should not be recorded for C.12.x entries.

    Example #5:
    Transfer from one oil residue (sludge) tank to another oil residue (sludge) tank, both listed under item 3.1 in the Supplement to the IOPPC

    Example #6:
    Incineration of oil residue (sludge) in Incinerator

    Example #7:
    Burning of oil residue (sludge) in Boiler

    Example #8:
    Evaporation of water (disposal) from an oil residue (sludge) tank listed under items 3.1 in the Supplement to the IOPPC

    Example #9:
    Regeneration of fuel oil from oil residue (sludge)

    Usage of code D: Non-automatic starting of discharge overboard, transfer or disposal otherwise of bilge water which has accumulated in machinery spaces.

    • Item No 13. Quantity discharged, transferred or disposed of, in m3
    • Item No 14. Time of discharge, transfer or disposal (start and stop).
    • Item No 15. Method of discharge, transfer, or disposal:
    1. Through 15 ppm equipment (state position at start and end);
    2. To reception facilities (identify port);
    3. to slop tank or holding tank or other tank(s) (indicate tank(s); state quantity retained in tank(s), in m3

    Example #10:
    Pumping of bilge water from engine-room bilge wells to a tank listed under item 3.3 in the Supplement to the IOPPC

    Example #11:
    Transfer of bilge water between tanks listed in item 3.3 in the Supplement to the IOPPC

    Example #12:
    Pumping of bilge water overboard from tank listed in item 3.3 in the Supplement to the IOPPC

    Example #13:
    Disposal of bilge water from tank listed in item 3.3 in the Supplement to the IOPPC to oil residue (sludge) tank listed in item 3.1 in the Supplement to the IOPPC

    Usage of code E: Automatic starting of discharge overboard, transfer or disposal otherwise of bilge water which has accumulated in machinery spaces.

    • Item No 16. Time and position of ship at which the system has been put into automatic mode of operation for discharge overboard, through 15 ppm equipment.
    • Item No 17 .Time when the system has been put into automatic mode of operation for transfer of bilge water to holding tank (identify tank).
    • Item No 18 .Time when the system has been put into manual operation

    Example #14:
    Pumping of bilge water overboard via 15 ppm equipment from tank listed in item 3.3 in the Supplement to the IOPPC or from engine-room bilge wells

    Example #15:
    Transfer of bilge water from engine-room bilge wells to a tank listed under item 3.3 in the Supplement to the IOPPC

    Usage of code F: Condition of oil filtering equipment.

    • Item No 19.Time of system failure.
    • Item No 20. Time when system has been made operational.
    • Item No 21. Reasons for failure.

    Example #16:
    Failure of Oily Filtering Equipment, Oil Content Meter or stopping device –

    Note: The condition of the oil filtering equipment also covers the alarm and automatic stopping devices, if applicable.

    A code ‘I’ entry should also be made indicating that the overboard valve was sealed shut due to non working Oil Filtering Equipment or Oil Content Meter. On the date where the system is functional again, a new entry, using code F 19 / 20 / 21 should be made where F 19 is the date and time of the initial failure and F 20 is the time the system is functional again.

    • When proper operation of the Oily Filtering Equipment, Oil Content Meter or stopping device is restored -.

    Note: The condition of the oil filtering equipment also covers the alarm and automatic stopping devices, if applicable. A code ‘I’ entry should also be made indicating that the overboard valve was unsealed since the operation of the Oil Filtering Equipment or Oil Content Meter has been restored.

    Usage of code G: Accidental or other exceptional discharges of oil.

    • Item No 22. Time of occurrence.
    • Item No 23. Place or position of ship at time of occurrence.
    • Item No 24. Approximate quantity and type of oil.
    • Item No 25. Circumstances of discharge or escape, the reasons there for and general remarks.

    Example #16:
    Accidental Pollution-
    Note: If failure of Oil Filtering Equipment or Oil Content Meter related equipment is involved, appropriate (F) entry is to be made in ORB. Relevant sections of the SOPEP (SMPEP) are to be used to combat oil spills at sea. Examples of Circumstances of discharge include, but are not limited to:
    1. Oil Content Meter failure.
    2. Fuel tank overflow.
    3. Ruptured bunkering hose/flange.
    4. Fuel tank leakage (due to collision or grounding).

    Usage of code H: Bunkering of fuel or bulk lubricating oil.

    • Item No 26.1.Place of bunkering.
    • Item No 26.2 Time of bunkering.
    • Item No 26.3. Type and quantity of fuel oil and identity of tank(s) (state quantity added, in tons, and total content of tank(s)). .
    • Item No 26.4 Type and quantity of lubricating oil and identity of tank(s) (state quantity added, in tons, and total content of tank(s)).

     Example #17:
    Bunkering of Fuel oil

    Example #18:
    Bunkering of Bulk Lubricating oil Note: Separate entries required for each grade of fuel oils and lubricating oils respectively to ensure transparency. This entry is not required if lubricating oils are delivered onboard in packaged form (55 gallon drum, etc.).

    Usage of code I: Additional operational procedures and general remarks.
    Example #20:
    Pumping oily bilge water from a Cargo Hold bilge holding tank to a tank listed under item 3.3 in the Supplement to the IOPPC
    Note: Any collection and transfer of oily bilge water into the engine-room bilge holding tank(s) from a cargo hold bilge holding tank(s) should be recorded using code (I) Tankers with slop tanks

    Example #21:
    Entry pertaining to an earlier missed operational entry Note: Date (1) to be the date of the original operation. Date (2) to be the current date i.e. the date the entry is made. Signed (1) Signature of Officer making I entry Signed (2) Signature of Officer making missed entry

    Example #22:
    De-bunkering of Fuel oil Note: Include receipt & certificate from receiver for amount & type of fuel oil de-bunkered.

    Tankers with slop tanks

    Example #23:
    Transfer of sludge from engine-room oil residue (sludge) tank to deck/cargo slop tank

    Example #24:
    Transfer of bilge water from tank listed in item 3.3 in the Supplement to the IOPPC to deck/cargo slop tank. Note: Requires this method listed in the IOPP Supplement under item 3.2.3. If non-oil-cargo related oily residues are transferred to slop tanks of oil tankers, the discharge of such residues should be in compliance with Regulation 34. (UI 22.1.1 for Regulation 15). Requires an entry in the Oil Record Book – Part II using code (J). If sludge or bilge water is transferred from multiple tanks in engine-room a separate entry must be made in ORB Parts I & II for each transfer.

    General Guidance – Additional Voluntary Recordings

    Example #25:
    Voluntary declaration of quantities retained in bilge water holding tanks ref. MEPC.1/Circ.640 – record weekly

    Example #26:
    Optional sealing of MARPOL Annex I related valve and/or equipment

    Example #27:
    Breaking of optional seal on MARPOL Annex I related valve and/or equipment

    (Source: MEPC1/CIRC.736.REV.2)

     

    Summary Oil Record Book (Part 1) Entries:

      • 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

    To get the clear information, please follow the below link:

    • https://www.ukpandi.com/fileadmin/uploads/uk-pi/LP%20Documents/Tech_Bulletins/Tch%20Bulletin.35(amd).pdf
    • https://www.uscg.mil/hq/cgcvc/cvc/marpol/sdoc/MEPC_1_Circ_736_rev_2.pdf

PORT STATE CONTROL (PSC)

F R Chowdhury


Image Credit: ClassNK

1. What is PSC:
It is customary to respect law of the land. You will appreciate that I will have to comply with laws of Malaysia so long I am in Malaysia no matter what my nationality is. The principle of Port State Control is based on this simple philosophy. A ship that enters my waters will have to comply with my legal requirements and standards. You might wonder as to how many countries’ laws the ship has to comply with? Fortunately the national laws are based on requirements of common international conventions. This means to say that the requirements relating to safety, security and protection of marine environment are derived from common international conventions and as such are similar to each other’s.
This amounts to say that all merchant ships trading around the world have to comply with minimum standards specified in international conventions. Ships will have to meet national standards (whichever flag they are registered in) and when abroad will have to meet the standards of the trading partner. With checks at both ends there is no room for rogue ship-owners to operate. This is how the world of shipping is expected to reach a level of ever higher standards.

2. Spirit of cooperation:
PSC does not mean tit for tat. “You detain my ship and now I detain your ship”. – No, it is not that. It is rather “Don’t worry. You may not be there. I will be there to ensure the safety of your ship and crew.” All responsible administrations have the same common goals and through FSI (Flag State Implementation) and PSC (Port State Control) they achieve the same. FSI and PSC are complimentary to each other to achieve safer and cleaner sea.

3. International instruments that make reference to PSC:
All major international conventions have reference to the provision of port state control. The philosophy is: it applies to own ships (wherever they may be) and other ships when in my waters. This is how it is imposed on one and all equally. The major international conventions that make reference to PSC are:

a) International Convention on the Law of the Seas, 1982 (UNCLOS-82);
b) International Convention on Safety of Life at Sea, 1974 (SOLAS-74);
c) International Convention on Prevention of Pollution at Sea, 1973/ 78 (MARPOL-73/ 78);
d) International Convention on Standards of Training, Certification and Watch-keeping for Seafarers, 1978 (STCW-78);
e) International Convention on Load Lines, 1966 (LL-66);
f) Int. Con. On Civil Liability for Oil Pollution Damage, 1969 (CLC-1969-92);
g) International Convention on Prevention of Collision at Sea, 1977 (COLREG-77);
h) International Convention on Ballast Control and Monitor, 2004 (BWCM-2004);
i) International Maritime Labour Convention, 2006 (ILO-MLC-2006).

4. Standards higher than Convention requirements:
Every member state has the right to set a level of standards higher than the convention requirements. Such higher standards may only be applied to their own ships. Convention does not allow a member state to impose such higher standards to visiting foreign ships. Being a party to a convention means a commitment to implement, support and promote the convention requirements and standards.

However, this should not be confused with the inherent right of a sovereign state to make their own law to apply to all if the state is convinced that such requirement is in the common interest. However, such law should have no reference to any international instrument.

5. National legislation implementing international conventions:

A sate is governed by its own laws. The court recognises national laws published in the official gazette. It does not go by what any official may sign abroad.

However, once a state becomes a party to an international convention, it can freely refer to various provisions of the convention in its legislation. As a matter of fact, it is a better way of drafting legislation rather than re-writing the entire convention again. However, certain things are not specified in the convention. They are for each state to do their own way. Those points must be covered otherwise the law will remain incomplete. The law must make a focal administrative authority responsible for its execution and compliance including issue of any exemption, equivalence etc. The law must have appropriate penal provision.

6. Ships flagged under non-party states:

While exercising PSC, shall we exonerate ships that fly flag of states that are not party to any specific convention? No, if such ships are allowed to get away with their deficiencies on the plea of not being a party to the convention then the spirit of the convention shall be defeated. The world will be full of sub-standard ships. That is why the convention stipulates that no favourable treatment shall be given to ships of non-party states. They will have to meet the same standards. This is a unique way to bring states under the conventions and ensure compliance of required standards by all ships. In other words, it means global compliance of convention standards.
7. Ethical principle of practise before preach:

There is something known as FSI (Flag State Implementation). It is the duty of the national administration to ensure that all ships under its flag comply with convention standards. The Flag Administration have jurisdiction over its own ships wherever they may be. The Administration can inspect its ship at random in addition to the requirements of statutory survey and certification. This is one way to ensure that ships maintain the highest standards of safety at all times. The Administration can then stand high above head and shoulders to say that it preaches what it practices and that there is no double standards. Importance of life and environment is equally important whether on own ships or foreign ships.

8. National maritime administration and Port authority:

The term “Port State Control” has nothing to do with Port Administration. The responsibility rests with the Administration of the state to which the port belongs. Port authority shall keep Administration informed of ships’ movement. The Administration shall then decide which ships it would like to inspect. The decision shall be based on various factors:

a) Flag of the ship and its reputation;
b) Age of the ship;
c) The RO (society it is classed with) and class records;
d) Any previous history of PSC detention;
e) If operating under any MOU then any exchange of information;
f) Any complaint or any other report.

9. Limited role of port authority:

The port authority cannot conduct PSC because of conflict of interest. Supposing that the Port Authority was allowed to conduct the PSC, then the Harbour Master could detain a ship with minor deficiencies and then charge the ship for over stay to make additional revenue earning for the port.

However, the Port Authority may like to see that the ship has sufficient insurance cover to pay for any harm or damage done to the port or environment. The pilot may confirm this as s/he boards the vessel and may refuse to handle the vessel that has no cover.

10. Role of Classification Societies:

PSC is essentially an Administration responsibility that cannot be delegated. The inspection is supposed to be free of charge and as such administration cannot ask someone else to do it. Besides a particular ship may have been certified by the relevant society and as such it cannot supervise its own work. As a matter of principle a classification society would not like to displease a ship-owner. So, ROs cannot be employed to conduct PSC.

However, relevant RO gets involved as soon as any deficiency is noted. The Society will ensure that all appropriate actions are taken to put the ship back in good order as it existed before the deficiency was noted. In some cases new certificates are issued (after restoration work is satisfactorily completed).

11. MOU:

The term MOU means Memorandum of Understanding. It is normally a regional agreement among a number of neighbouring states to conduct PSC in a coordinated manner. MOU normally has a secretariat which maintains all necessary data and through this centre they exchange necessary information. If a vessel is released from previous port with a commitment to conduct repairs next port, the information is relayed accordingly. If the vessel does not turn up in next port, she may even be banned from entering the MOU region. If a ship has been inspected in previous port with no deficiency then the information is available to avoid any duplication. This is how MOU saves time and energy but makes coordinated action more effective. MOU also gives the opportunity to share knowledge and experience.
Each MOU Secretariat develops its own convenient reporting form in the shape of check-list. A number of easy to understand codes are used. There is also additional space to write important observations to complement the check-list. On return to office the surveyor feeds the report on the computer and all MOU states get to see and know.
However, it must be understood that international conventions make no reference to MOU. These are voluntary regional agreements based on common requirements and understanding to facilitate coordinated operation of PSC. The United States (USA) is not a party to any MOU. It operates PSC on its own. Canada is a party to two MOUs – one for Atlantic region (Paris MOU) and other for Pacific region (Tokyo MOU).

12. Three stages of PSC:

There are three logical stages of PSC. They are:

a) Certificates and documents – whether the ship has all statutory certificates, documents and other information valid and up to date;
b) Whether all machinery and equipment are in Good Working Order;
c) If the crew are well trained and familiar with their assigned responsibilities.
It is not necessary that all three stages will always be carried out. The surveyor should be competent enough to know and understand in each case how essential it is to progress further.

13. Three categories of report:

On conclusion of the inspection there could be one of the three types of reporting:
a) Clean report – no deficiency;
b) Minor deficiency – not serious enough for detention. There are again two courses of action – to give a warning that vessel must not come again with such deficiency – to attach a condition that deficiency must be rectified within a period, preferably in next port. Next port or MOU members must be notified.
c) Detention – serious deficiency leading to detention.

14. Detention:

Detention is justified only when the inspector is convinced that allowing the ship to proceed to sea may endanger life, property or environment. However, vessel should be allowed to proceed to a port with necessary repair facilities if such facilities are not available in the port of inspection. In extreme cases ship may be advised to carry some substitute equipment for such journey.

Since detention may eventually lead to legal challenge, the detention notice must also make reference to provisions of national law in addition to convention requirements.

Ship shall be served with a detention notice. It is for the ship to let owners/ managers, agents and RO/ Classification Society know about it. PSC authority shall notify flag state or their local mission. In order that the detention is duly enforced the authority shall also notify port and customs authority as well as the Coastguard.

15. Difference between arrest and detention:

Detention by PSC inspector is an administrative action permissible under the law for reasons of safety whereas ships may be arrested by a court order against any claim. Arrest of ship is a judicial matter.

16. Can fine/ penalty be imposed for deficiencies found under PSC?

No, ships may only be detained until it is made safe to proceed to sea. No judicial measure need to be taken. The question of imposing fine/ penalty does not arise and is not permissible.

17. Can the Administration charge fees for PSC inspection?

No, PSC inspections are done for reasons of safety. It is humanitarian service to protect life and environment. Ship-owner cannot be charged because they never asked for such inspection.

However, when the ship asks for a further visit of a surveyor/ inspector to give clearance certificate, it will be justified to charge for such services.

18. What PSC means to seafarers:

Seafarers want to sail on a safe ship. A good PSC inspection goes a long way in making the ship safer. Seafarers must provide full cooperation to PSC inspector in their own interest.

19. How to avoid PSC detention:

Ships should comply with all applicable requirements and maintain to the highest standards of safety and pollution prevention. A list of certificates and documents is attached herewith. Ships should comply with those requirements that apply to them.

20. Good governance by Administration:

Every Flag State should be concerned about their own reputation. It is important that following points are taken into account:

a) Be a Party to all applicable International Conventions and Protocols;
b) Appropriate legislation giving force of law to applicable provisions of international instruments;
c) Well trained and competent persons in the Administration;
d) Documented procedures for major operational matters;
e) Conduct FSI and PSC with the same equal motive and goals;
f) Audit/ review of performance by ROs;
g) Maintaining highest standards of seafarers’ training and certification;
h) Inquiry/ investigation of accident/ casualty only to find root causes for possible improvement (no-blame culture ensuring that such inquiry should have no bearing on any judicial inquiry or right to sue each other for damages);
i) Record-keeping;
j) Periodical review of all activities and possible improvements.

(Second Edition, published by the author on 12-March-2017)

ENCLOSED SPACE ENTRY

By Maklub Al Mostofa

Enclosed Space:

For the purpose of this Guide, an ‘Enclosed Space’ is defined as a space that has the following characteristics:

  • Limited openings for entry and exit.
  • Unfavourable natural ventilation.
  • Not designed for continuous worker occupancy

Enclosed spaces include, but are not limited to:

      • Cargo spaces
      • Double bottoms
      • Fuel tanks
      • Ballast tanks
      • Cargo pump-rooms
      • Cargo compressor rooms
      • Cofferdams
      • Chain lockers
      • Void spaces
      • Duct keels
      • Inter-barrier spaces
      • Boilers
      • Engine crankcases
      • Engine scavenge air receivers
      • Sewage tanks

     

    Many of the casualties that have occurred in enclosed spaces on ships have resulted from people entering an enclosed space without proper supervision or adherence to agreed procedures. In almost every case, the casualty would have been avoided if the simple guidance in this Chapter had been followed.

    The rapid rescue of personnel who have collapsed in an enclosed space presents particular risk. It is a human reaction to go to the aid of a colleague in difficulties, but far too many additional and unnecessary casualties have occurred from impulsive and ill-prepared rescue attempts.

    Assessment of Risk

    In order to ensure safety, a risk assessment should be carried out. Gas tests carried out prior to entry into the space should reflect the contaminants that can reasonably be expected to be present within the space, taking into account the previous cargo carried, ventilation of the space, structure of the tank, coatings in the space and any other relevant factors.

    When preparing for entry into a ballast tank or void space where hydrocarbon vapours may not normally be present, it is prudent to test the space for hydrocarbon vapour or H2S if the space is adjacent to a cargo or bunker tank. This is particularly important if entry is being made to investigate the possibility of bulkhead defects.

    Respiratory Hazards

    Respiratory hazards from a number of sources could be present in an enclosed space. These could include one or more of the following:

    • Hydrocarbon vapours, such as butane and propane.
    • Toxic contaminants associated with organic vapours, such as aromatic hydrocarbons, benzene, toluene etc.
    • Toxic gases, such as benzene, hydrogen sulphide and mercaptans.
    • Oxygen deficiency caused by the presence of inert gas, oxidation (rusting) of bare steel surfaces, or by microbial activity.
    • Solid residues from inert gas and particulates, such as those from asbestos, welding operations and paint mists.

    Hydrocarbon Vapours

    During the carriage and after the discharge of hydrocarbons, the presence of hydrocarbon vapour should always be suspected in enclosed spaces for the following reasons:

    • Cargo may have leaked into compartments, including pumprooms, cofferdams, permanent ballast tanks and tanks adjacent to those that have carried cargo.
    • Cargo residues may remain on the internal surfaces of tanks, even after cleaning and ventilation.
    • Sludge and scale in a tank that has been declared gas free may give off further hydrocarbon vapour if disturbed or subjected to a rise in temperature.
    • Residues may remain in cargo or ballast pipelines and pumps.

    The presence of gas should also be suspected in empty tanks or compartments if non-volatile cargoes have been loaded into non-gas free tanks or if there is a common ventilation system which could allow the free passage of vapours from one tank to another.

    Toxic contaminants could be present in the space as residues from previous cargoes, such as benzene or hydrogen sulphide. To be considered safe for entry, whether for inspection, Cold Work or Hot Work, a reading of less than 1% LFL must be obtained on suitable monitoring equipment.

    Toxic Gases:

    • Benzene

    Checks for benzene vapour should be made prior to entering any compartment in which a cargo that may have contained benzene has recently been carried. Entry should not be permitted without appropriate personal protective equipment, if statutory or recommended TLV-TWAs are likely to be exceeded (see Section 2.3.3.2). Tests for benzene vapours can only be undertaken using appropriate detector equipment, such as detector tubes. Detector equipment should be provided on board all ships likely to carry cargoes in which benzene may be present.

    • Hydrogen Sulphide

    H2S is present in some crude oils and in some products in varying concentrations. Where the concentration is high, the oil is often referred to as being ‘sour’. H2S is very soluble in water. General practice and experience indicates that washing a tank with water after carrying a cargo containing H2S should eliminate the hydrogen sulphide vapour within the space.

     However, prior to entry into an enclosed space which has previously carried oil containing H2S, or where the presence of H2S vapour may be expected, the space should be ventilated to a reading of less than 1% LFL on a combustible gas indicator and tested for the presence of H2S using a gas detector tube. Care should be taken not to rely on the use of catalytic H2S sensors which may have a cross-sensitivity with hydrocarbon vapour. Since H2S is heavier than air, it is very important that the bottom of any space is thoroughly tested.

     When carrying a cargo containing H2S, particular attention should be given to the possibility of the presence of H2S in locations such as pumprooms, deck stores and in ballast tanks. There is a high probability of the presence of H2S in ballast tanks due to the gas being drawn into the tank when deballasting during the loading operation.

     Mercaptans

    Mercaptans are present in the vapours of pentane plus cargoes and in some crude oils. They may also be present where oil residues have been in contact with water for extended periods. The presence of Mercaptans can be detected by the use of chemical detector tubes. Their concentration should be reduced to 0.5 ppm to avoid discomfort to personnel and nuisance smells.

     Oxygen Deficiency

     Before initial entry is allowed into any enclosed space, the atmosphere should be tested with an oxygen analyser to check that the air contains 21% oxygen. This is of particular importance when considering entry into any space, tank or compartment that has been previously inerted. Lack of oxygen should always be suspected in all enclosed spaces, particularly if they have contained water, have been subjected to damp or humid conditions, have contained inert gas or are adjacent to, or connected with, other inerted tanks.

    Products of Inert Gas

    By-products of combustion when inert gas is produced from boiler flue gas or from an inert gas generator include carbon monoxide and carbon dioxide.

    Carbon monoxide is a toxic gas that may be present in cargo tank atmospheres following gas freeing and in spaces containing components of the inert gas plant. Carbon dioxide is not toxic, but presents a smothering hazard. Adequate ventilation is required to maintain a normal oxygen level in air of 21% by volume in the space and to eliminate any hazard.

    Atmosphere Tests Prior to Entry

     No decision to enter an enclosed space should be taken until the atmosphere within the space has been comprehensively tested from outside the space with test equipment that is of an approved type and that has recently been calibrated and checked for correct operation.

     The appropriate atmosphere checks are:

    • Oxygen content is 21% by volume.
    • Hydrocarbon vapour concentration is less than 1% LFL.
    • No toxic or other contaminants are present.

     Care should be taken to obtain measurements from a representative cross-section of the compartment by sampling at various depths and through as many deck openings as practicable. When tests are being carried out from deck level, ventilation should be stopped and a minimum period of about ten minutes should be allowed to elapse before readings are taken.

     Even when tests have shown a tank or compartment to be safe for entry, pockets of gas should always be suspected.

    If extensive work is to be carried out within a large space, such as a cargo tank, it is recommended that a full assessment of the tank atmosphere is undertaken after the initial tests have been satisfactorily carried out and recorded. The person undertaking the full assessment should enter the tank carrying an emergency escape breathing device and a personal gas monitor, in addition to the gas testing instrument. The tank atmosphere should be checked frequently during this entry, with particular attention being placed on testing the work location(s) and places that are inaccessible for testing from the deck. On satisfactory completion of this additional atmosphere test, the results should be recorded as required by the appropriate safety procedure in the Safety Management System.

    While personnel are in a tank or compartment, ventilation should be continuous. Regeneration of hydrocarbon gas should always be considered possible, even after loose scale or sludge has been removed. Continual checks on the atmosphere in the space should be made as specified in the Safety Management System.

     Atmosphere tests should always be made after any interruption or break in the work. Sufficient samples should be drawn to ensure that the resulting readings are representative of the condition of the entire space.

     When entering cargo and bunker tanks, all the tanks and spaces adjacent to the space to be entered should also be tested for hydrocarbon gas and oxygen content and, where appropriate, the inert gas pressure should be lowered to reduce the possibility of any inter-tank leakage. Notwithstanding this precaution, personnel should remain alert to the possibility of leakage of hydrocarbon gas from adjacent spaces or from pipelines running through the tank.

    Control of Entry into Enclosed Spaces

    It is the responsibility of the Company to establish procedures for safe entry of personnel into enclosed spaces. The process of requesting, raising, issuing and documenting permits to enter into an enclosed space should be controlled by procedures in the ship’s Safety Management System (SMS). It is the Master’s responsibility to ensure that the established procedures for entry into an enclosed space are implemented.

    The Master and Responsible Officer are responsible for determining whether entry into an enclosed space may be permitted. It is the duty of the Responsible Officer to ensure:

    •  That the space is ventilated.
    •  That the atmosphere in the compartment is tested and found satisfactory.
    •  That safeguards are in place to protect personnel from the hazards that are identified.
    •  That appropriate means for controlling entry are in place.

    Personnel carrying out work in an enclosed space are responsible for following the procedures and for using the safety equipment specified.

    Prior to entry into an enclosed space, a risk assessment should be completed to identify the potential hazards and to determine the safeguards to be adopted. The resulting safe working practice should be documented and approved by the Responsible Officer before being countersigned by the Master, who confirms that the practice is safe and in compliance with the ship’s Safety Management System. The permit, or other enabling document, should be sighted and completed by the person entering the space, prior to entry.

    The controls required for safe entry vary with the task being performed and the potential hazards identified during the risk assessment. However, in most cases, an Entry Permit System will provide a convenient and effective means of ensuring and documenting that essential precautions have been taken and, where necessary, that physical safeguards have been put in place. The adoption of an Entry Permit System, which may include the use of a check-list, is therefore recommended.

    Permission to continue work should only be given for a period sufficient to complete the task. Under no circumstances should the period exceed one day.

    A copy of the permit should be prominently displayed at the entrance to the space to inform personnel of the precautions to be taken when entering the space and of any restrictions placed upon the activities permitted within the space.

     The permit should be rendered invalid if ventilation of the space stops or if any of the conditions noted in the check-list change.

     Restricting the issue of approvals, such as entry permits, so that all cargo tanks which are safe to enter are shown on one document, may be found to simplify the paper administration, avoid overlapping and reduce the possibility of confusion as to which approval applies to which tank. However, if such a system is used, there must be rigorous control to ensure cancellation of existing permits, and that the atmospheres of all named tanks are correctly tested at the time of issue so that an effective extension of a period of validity does not occur by default. It will be particularly important to ensure that the permit process is supplemented by the marking of tank lids with notices indicating which tanks are safe to enter.

    Inspection of cargo tanks after cleaning and before loading can require an independent surveyor to enter the tank. All relevant tank entry procedures must be observed.

    Safeguards for Enclosed Space Entry

     Before allowing access to the space, the Responsible Officer should ensure that:

    • Appropriate atmosphere checks have been carried out.
    • Piping, inert gas and ventilation systems have been isolated.
    • Effective ventilation will be maintained continuously while the enclosed space is occupied.
    • Fixed lighting, such as air-turbo lights, are ready for extended entry periods.
    • Approved self-contained, positive pressure breathing apparatus and resuscitation equipment is ready for use at the entrance to the space.
    • A rescue harness, complete with lifeline, is ready for immediate use at the entrance to the space.
    • A fully charged approved safety torch is ready for immediate use at the entrance to the space.
    • A responsible member of the crew is in constant attendance outside the enclosed space, in the immediate vicinity of the entrance and in direct contact with the Responsible Officer.
    • All persons involved in the operation should be trained in the actions to be taken in the event of an emergency.
    • Lines of communications have been clearly established and are understood by all concerned.
    • Names and times of entry will be recorded and monitored by personnel outside the space.

    The personnel undertaking the task should ensure that such safeguards are put into effect prior to entering the space.

    The personal protective equipment to be used by people entering the space must be prescribed. The following items should be considered:

    •   Protective clothing including work clothing or protective suits, safety boots, safety helmet, gloves and safety glasses.
    •   For large spaces, or where climbing access will be undertaken, the wearing of safety harnesses may also be appropriate.
    •   Approved safety torches.
    •   Approved UHF radio.
    •   Personal gas detector or an area gas detector and alarm.
    •   Emergency Escape Breathing Device(s).

    Evacuation from Enclosed Spaces

    If any of the conditions that are stated on the permit for entering the space change, or the conditions in the space are suspected of becoming unsafe after personnel have entered the space, personnel should be ordered to leave the space immediately and not be permitted to re-enter until the situation has been re-evaluated and the safe conditions stated on the permit have been restored.

    Sample of Enclose Space Entry:

     

    You can read more by following the below link:

    • http://www.westpandi.com/Publications/News/Archive/IMO—Revised-Recommendations-for-Entering-Enclosed-Spaces-aboard-Ships/
    • http://www.standard-club.com/media/24153/AMastersGuidetoEnclosedSpaceEntry.pdf

LNG SHIPS

By F. R. Chowdhury

images
Image Credit: Liquefied Gas Carrier.com

Properties of LNG:

LNG is actually METHANE. Purity of cargoes ranges from 67% to 99.5%, according to geographical location. Impurities consist mainly of Ethane and Propane. LNG is:
Non – toxic
Non – corrosive
Colourless
Odourless
In its gaseous form it is lighter than air. Its ratio of volume as liquid to gas is 1:600.

Lower flammable limit is approx. 4% in air. Upper flammable limit is approx. 14% in air. There is no LEL or UEL as such because there is no explosive effect upon ignition at any concentration. Auto ignition temperature is approx. 585° C and there is therefore little chance of ignition from engine or boiler exhausts. Methane has a slow travelling flame front and can be effectively extinguished with dry powder. Ship superstructure or other vulnerable areas may be protected by water spray, which imparts heat to the vapour cloud, resulting in immediate upward evaporation. CO2 injection firefighting systems are not fitted due to the possibility of ignition by static electricity being generated.

Because it is odourless and colourless it presents additional dangers to ships crew who may be unaware of system leaks. An odour is given to the gas prior to domestic distribution to enable detection by smell. This process is known as “stenching”.

Containment Systems / Ship Types:

There are basically two types of tank construction in current use. They are the MOSS ROSENBURG and MEMBRANE systems. In both cases the containment system is designed to serve two purposes:

• To contain LNG cargo at cryogenic temperature (-160 degree C);
• To insulate the cargo from hull structure.

The MOSS – ROSENBURG system comprises usually of four aluminium alloy spherical tanks, the upper half of which protrude above the main deck. The tanks are connected to ship’s structure by a skirt extending downwards from the equator of the tank into the hold space. Insulation is applied around the spherical tank and is backed by aluminium foil, which forms a spray shield in case of leakage. Accumulated leakages may be collected in a simple drip tray arrangement below the tank, designed to protect the structure below from excessive cooling. Minor leakage would flash off rather than form any significant pool. Tank thickness ranges from 30 – 50mm top to bottom but with a thickness of about 120mm at the equatorial ring. These tanks suffer relatively few structural problems. However MOSS ships require significant reinforcement of structure at sheer strakes and utilise a trunk deck construction at either side. In fact the hull construction is remarkably similar to a container ship in this regard, but with massive stiffening at the trunk deck. Severe rolling of the vessel is not unusual, especially in ballast condition. Numerous ballast tanks are fitted. A MOSS hull results in a higher GT compared to Membrane type ships. e.g. 120,000 compared to 92,000 GT.

MEMBRANE tanks vary in design according to manufacturer but all designs follow similar basic principles of construction. There is a primary barrier made of “Invar” or stainless steel, which forms the cargo tank surface. This is 0.7 or 1.2 mm thick, depending on design, and is backed by insulation blocks of approx. 250mm thickness. A secondary barrier sits behind this, made of Invar or Triplex (Aluminium / Glass fibre cloth composite), again depending on design. The secondary barrier is backed by more insulation, which directly sits against the ship’s hull structure.

The tank lining thus consists of two identical layers of membrane and insulation, so that in the event of any leak in the primary barrier, the cargo is contained by the secondary barrier. The secondary barrier is only designed to contain any envisaged leakage of cargo for a maximum period of 15 days (IGC Chapter IV/ 4.7.4). This system ensures that all the hydrostatic loads of the cargo are transmitted through the membranes and insulation to the inner hull plating of the ship.

MEMBRANE ships are prone to sloshing damage at certain loaded conditions. As a result, insulation boxes and adjacent cofferdam structures have been reinforced on ships built 2003 onwards. Loading was previously prohibited between 10% of tank length (expressed as a height of the tank) and 80% tank height. Later ships are now restricted loading between 10%L and 70%. This small improvement allows all four tanks to comply with restrictions on loading height by simple transfer of cargo for any tank condition.

A large amount of high tensile steel is used in construction of LNG ships. The current ceiling on ship capacity (approx. 140,000 cu.m) is the result of Japan, the major gas importer to date, imposing a 105,000 dwt limit on ships entering its ports. With expanding markets, ships up to 216,000 cu.m are planned.

Ship operations:

Where a tanker has been designed specifically to carry fully refrigerated Ethylene (boiling point at atmospheric pressure of -104 degree C) or LNG (atmospheric boiling point -162 degree C) nickel-alloyed steel, stainless steel (such as Invar) or aluminum must be used as tank construction material.

LNG is loaded at a temperature of –162° C and at atmospheric pressure. Tank pressures are maintained at slight positive pressure but below 230 mbar (Cargo tank relief valve setting). A small percentage of the cargo boils off over the voyage (can be as low as 0.15% of the cargo per day) and this is normally burnt in the ship’s boilers, generating steam for use in the steam turbine propulsion plant. Because of the boil-off occurring, Administrations may allow filling up to 99.5% of tank volume instead of the 98% stipulated maximum. This is not normally a problem for “Moss” ships due to their spherical tank construction and highly accurate measurement due to the shape of the tank. “Membrane” ships with their flat topped cargo tanks may not be so accurately measured for certain ship conditions of list and trim.

All ships are fitted with a Nitrogen generator for inerting pipes, void spaces and membrane spaces as necessary. (Safety note: Asphyxiation by nitrogen is swift, due to there being no CO2 present in the lungs. There is no stimulus to breathe and you simply drop dead). In the case of membrane ships, a traditional inert gas generator is not required due to the nature of operations and construction. Moss ships require an inert gas generator to flood the hold spaces surrounding the spherical tanks in case of gas detection only. Otherwise these spaces may be filled with dry air.
Relief valves are fitted not only to cargo tanks and membrane spaces, but also to all liquid lines between isolating valves. Consequently, surveyors might require a sample test only of relief valve operation.

Cargo discharge is by submerged electric motor driven centrifugal pump, two per tank each rated at 1700 cu.m/hr.

Cargo boil-off is initially controlled by the thickness of insulation that is fitted to the tank. The required thickness is affected by the calculated amount of boil off required for propulsion. The ship is usually employed on the same route for life and so the boil off may be determined by the owner/charterer as a trade off between anticipated price of LNG and fuel oil and also earning capacity of the ship by comparing % boil-off to cargo delivered. (Less insulation means more cargo capacity but also more cargo lost by boil-off). The Charterer will daily instruct the ship to burn LNG or fuel oil, depending on current or anticipated market prices. Ultimately, minimum insulation thickness is determined by IGC Code requirements, which are designed to protect the ship’s structure from excessively low temperatures. Ships are fitted with regasification plant to generate more gas for propulsion, in the event of boil-off being insufficient.

Boil-off cannot simply be vented in case of overpressure. IGC Code requires that this ozone depleting substance be dealt with at all times. In case of boil-off being in excess of propulsion requirements, the usual method is to simply generate and dump steam to the condenser. Dual fuel diesel engine technology has arrived and it is likely to become more popular. It is also now economically feasible to reliquify the gas on board and return it to the cargo tanks. This raises questions on dealing with excess boil-off in case of non-propulsion or reliquifaction plant breakdown. (At a cost of $10,000,000 it is likely that only one will be fitted per ship). An answer has been offered by industry in the form of an LNG burner that simply burns the gas to atmosphere. They are known by several fancy names, principally to disguise the fact of their wasteful purpose. A design for a 210,000 cu.m ship has a 6m diameter flue!

A question over allowable maximum tank filling also arises due to possibility of no boil-off. (Value of LNG cargoes is rising rapidly and may outstrip fuel oil prices – LNG might not be used for propulsion). The possibility of returning liquefied gas to an already full tank should also be considered.

LNG overflowing from a mast riser can easily crack deck plating. Although it can be demonstrated that LNG spilt onto steel plate will not cause cracking, actual cases have shown that deck plating can and will crack due to inherent stresses generated by fabrication of the hull and/or ship in loaded or ballast condition. In the case shown on the LNG course, multiple cracks propagated completely through under-deck stiffeners.

Statutory considerations:

LNG ships are often built to USCG rules (CFR) in addition to IMO/IGC Code requirements in order to trade to US. All ships have instrumentation in excess of statutory requirements and failure of one instrument will not usually render the ship non-compliant.

LNG ships are traditionally drydocked at 30 month intervals, at which time instrumentation is overhauled by requirement of the shore terminals. Instrumentation includes the Custody Transfer System (CTS); a computerised monitoring system, which enables monitoring of the ship condition by the shore facility, with Emergency Shut Down of ship cargo operations being possible from ashore also. CTS are not a statutory or class requirement.

With markets changing, it is anticipated that owners operating particularly in the spot market may object to taking their ships out of service when an in-water survey might possibly suffice. It is therefore expected that pressure to have in-water surveys carried out at intermediate surveys will be forthcoming. Currently Class intermediate surveys are required to be carried out while the ship is gas-free and ships are usually in drydock as a consequence of shore terminals requirements stated above.

The expected expansion in the LNG fleet will require 5000 additional crew with relevant STCW endorsements. Also of concern is the emergence of new technology. Gas turbines are expected to become increasingly used in LPG ships and the question was asked, “What will Flag States require by way of training” for new technology such as this?

LNG ships are known to be positioning themselves to take advantage of possible spot cargoes, and switching off AIS to maintain their commercial advantage.

Prior to delivery, LNG ships have functional gas trials carried out with a usually small partial load in order to prove satisfactory operation of cargo systems and instrumentation.

Upon delivery, newly built LNG ships have three IGC Code items outstanding:

• Initial loading
• Initial discharge
• Cold spot inspection

One IACS Society has stated that these three items may be considered to be completed during gas trials. Other member societies disagree with this view and an IACS UI (unified interpretation) is under consideration. Some ships carry out gas trials fully loaded but it is important that the cold spot inspection is not carried out before the thermal inertia of the insulation has been overcome.

Some gas leakage into the space behind the primary membrane is allowable. The alarm level to be set at 30% LFL or up to 30% by volume, (well above the flammable range) depending upon the type of containment system fitted. The wide range of allowable limits is principally because early containment systems leaked anyway! Leakages into the space are normally purged with nitrogen and are not perceived to be a real danger to the ship.

The first Gas Code for existing ships was retrospectively written and applies to ships pre 1975. The next Gas Code applies to ships 75-85 and the current IGC Code applies to ships ‘86 onwards.

Ship systems and design are rapidly changing and the current IGC Code is out of touch with developments in some areas. Consequently LR is adopting a risk-based approach for some new designs and have already applied risk based analysis to gas turbine and dual fuel technology in the absence of existing regulations.

Future developments:

Future developments include “Gas to Liquid” conversion of LNG to pure diesel oil, naptha etc. This is a chemical process.

Shipping developments include proposed Compressed Natural Gas Ships (Cargo 70-80 bar pressure), Compressed LPG Ships (cargo at up to 250 bar pressure) and “Gas to wire” offshore generating stations, which may be classed and registered in the same way as FPSO vessels currently are.

LNG Course:

Operation of Liquefied Gas Carriers involves potential hazards. Training in emergency procedures and use of special emergency equipment must be given to crew. The technical complexity of design, construction, operation and maintenance require good training. The training must help in understanding of LNG ship technology and ship operations including considerations for loading in excess of 98%.

STCW training & endorsement:

Regulation V/1-2 states: Officers and ratings assigned specific duties and responsibilities related to cargo or cargo equipment on liquefied gas tankers shall hold a “Certificate in Basic Training for liquefied gas tanker cargo operations”.

This basic certificate may be obtained either by completing at least three months service on a liquefied gas tanker followed by successful assessment of competence meeting the requirements of Code A-V/1-2 paragraph 1. Or by having successfully completed an approved course of training meeting the same requirements (A-V/1-2, paragraph 1).

Management level officers and any person with immediate responsibility for loading, discharging, care in transit, handling of cargo, tank cleaning or other cargo related operations on liquefied gas tankers shall successfully complete an approved advance training for liquefied gas tanker cargo operations and complete a minimum period of three months service on a liquefied gas tanker in a supervised capacity (other than management level).

Administration shall issue Certificate of Proficiency to those who meet the requirements for certification under both categories.

[Please note this article does not meet any training requirement. This article merely presents an outline/ introduction of LNG ships for basic knowledge.]