SHIELD METAL-ARC WELDING (SMAW)


In shielded metal-arc welding, the intense heat from an electric arc is used to melt and fuse metals to form a weld. It is one of the oldest and most widely used welding processes. Although used chiefly for joining iron and mild steels, shielded metal-arc welding is well suited to maintenance tasks because the equipment is relatively inexpensive, simple to operate, and can be used for welding many different kinds of metals.

Below, you will find explanations describing the shielded metal-arc welding process and how the welding machines and accessories are set up and used. You will also find information on selecting an electrode. The personal safety equipment and precautions are also described.

HOW THE PROCESS WORKS
A typical SMAW outfit consists of an electric welding machine, two welding cables, a ground clamp, an electrode holder, and a covered metal electrode. Electric current from the welding machine is used to form an electric arc between the tip of the electrode and the work.



Welding is started by touching the end of the electrode to the base metal, then lifting the electrode about ¼ inch. This forms the arc, which produces temperatures up to 5550°C. The intense heat at the arc area instantly melts the base metal and begins to burn the covering off the electrode and melt the core. The melted core becomes filler metal for the weld and the decomposition of the flux forms a protective gaseous atmosphere around the arc area. The gas forms a shield against contamination from oxygen and nitrogen in the surrounding air. Additional shielding is provided by the electrode flux, which forms a deposit called slag.

The shielding gas is ionized, and conducts electricity and maintains the stability of the arc.

WELDING VOLTAGE AND CURRENT
Either direct current (DC) or alternating current (AC) is used. The arc voltage or working voltage is the voltage present in the welding circuit while an arc is struck and welding is being done. The arc voltage ranges from 15V to 40V depending on the arc length.

The open circuit voltage is the voltage generated by the welding machine when no welding is being done. Open-circuit voltages are normally set between 50V and 100V, but drops to the arc voltage level when an arc is struck and welding begin.

ARC LENGTH
In any electrical circuit, there is a correlation between the voltage, current and the resistance. The best results are normally obtained with an arc length about the diameter of the electrode.

When the arc length is increased, less current flow occurs because of the increased resistance. The result is a cooler arc and a greater tendency to spatter. There will be less penetration of the weld, increased exposure to oxidation and contamination, and an erratic, unstable arc.

When the arc length is reduced, less resistance more current flows with less voltage and the arc becomes hotter. With thin material, the heat can melt a hole in the welding, porosity, and undercutting of the adjacent base metal.

POLARITY
For DC machines, this is important. When the electrode is negative and the work piece is positive, this is called Straight Polarity. The opposite of this is Reverse Polarity.

DCSP or direct current straight polarity is characterized by faster melting of the electrode, the weld puddle being broad and penetration into the base metal is relatively shallow. This is used when fast welding speeds and high deposition rates are required.

DCRP or direct current reversed polarity results in a hotter arc, making deeper, narrower weld puddle. This is used for structural welding, multi pass welds, and applications requiring deep penetrations.

Most electrodes are designed to be used with only one polarity.

POWER SOURCES
Most AC power sources contain a transformer that steps down line voltage to the level required for welding (normally less than 100V)

WELDING MACHINES
Many types and sizes of welding machines are used for shielded metal-arc welding. The current of a Constant-Current type does not change significantly in variations in arc length. This is preferred for manual welding operations.

The Constant-Potential type of welding machine adjusts the current according to the arc length. If used in a manual operation, the unavoidable variations in arc length will produce large fluctuations in the current, resulting in an unstable, non-uniform arc. For automatic operations, the constant electrode feed rate establishes a stable arc and uniform arc length.

The current rating of the machine is its maximum current output. A current rating of 400 amp means the machine can deliver up to 400 amps of welding current.

The duty cycle rating of the machine is the safe operating capacity for non-stop welding. This is expressed as a percentage over a 10-minute period over which a machine can deliver its rated maximum welding current output without damage or overheating. An 80 percent 400-amp machine is one, which can deliver 400 amps of welding current for a total of 8 minutes out of every 10, and must idle at least, 2 minutes out of every 10 for cooling.

TOOLS AND ACCESSORIES
The tools for SMAW are: cables, holders, clamps, chipping hammer, wire brush. The protective equipment are face shield, goggles, apron, gloves, shoes, long sleeved shirt. The protective equipment is to avoid eye injuries, and burns. Also there is a need to prevent electric shocks, especially in wet areas.

SELECTING AN ELECTRODE
Electrodes are classified by their core material: mild steel, high-carbon steel, special alloy steel, cast iron, and non-ferrous. Mild steel electrodes are the most commonly used. In general, the electrode core material is matched as closely as possible with the composition of the base metal. Electrode size varies with the thickness of the base metal.

The size and characteristics of the selected electrode determine the arc current settings on the welding machine. Normally, the range of recommended amperage for the electrode is given by the manufacturer.

SET UP AND OPERATION
Observe fire precautions before starting to weld. No combustible should be near the work area. 

With the electrical power still off; clamp the earth wire to the work piece and the electrode on the holder. Turn on the power. To strike an arc, position the end of the electrode about 1 inch above the weld start point. Lower your face shield and with a rapid tapping of scratching motion, touch the electrode to the base of the metal. Immediately after the contact, raise the end of the electrode slightly to establish an arc whose length is approximately equal to the electrode diameter.

If you do not raise the electrode fast enough, it will stick to the work. Twist or bend the electrode to break it free. If the electrode does not break free, quickly release it from the holder. With a little practice, you can learn to strike an arc without the electrode sticking.

When the current settings and a proper arc length is maintained, a continuous cracking sound is heard while welding. A humming sound indicates that the arc length is too long or the current is too high. Arcs too short make a popping sound and may flash on and off, indicating the electrode is sticking and short circuiting to the base metal.
Friday, August 23, 2013
Posted by Unknown
Tag :

HEAT EXCHANGERS


A heat exchanger is a piece of equipment in which two fluids are separately circulated
in adjacent spaces so that some of the heat in the fluid at the higher temperature is transferred into the fluid at the lower temperature. The fluid having the higher
temperature is therefore cooled and the fluid having the lower temperature is
heated.

The heat from a fluid can therefore be transferred to another colder fluid by means of:
    a.  Separately circulating them in adjacent spaces.

b.  Mixing them together.                                                       

Surface heat transfer is defined as heat flowing from a “hot” fluid through a tube wall or other membrane to another cooler fluid.

Contact heat transfer is defined as heat flowing from a hot fluid to a cooler fluid due to mixing of one with the other.

A heat exchanger is a device for transferring thermal energy from one medium to another. It generally consists of two channels or system of channels, one for each medium, and separated from each other by partitions through which heat is transferred from the hot medium to the cold medium.

Most coolers used on board ship transfer heat from a hot fluid to sea water. For the main propulsion engine of the motor ship, the engine jacket water, lubricating oil and charge air must be cooled and generally also water or oil used in cooling the pistons. In a steamship, apart from the heat yielded to the main condenser, the turbine and gearbox lubricating oils provide the principal sources of heat rejected to the circulating cooling water. Auxiliary prime movers require cooling and air compressors have intercoolers and aftercoolers.

Steam heated heat exchangers include heavy fuel oil heaters, boiler air pre-heaters, units to heat sea water for tank washing, evaporators, feed heaters and calorifiers.

Shipboard heat exchangers may therefore be classified under the following categories:

COOLER
The temperature of a hot liquid is lowered by transferring part of its heat to sea water.

CONDENSER
Heat from a hot gas or vapour is transferred to seawater to the extent that the gas or vapour liquefies.

HEATER 
The temperature of a liquid or gas is raised by transferring heat energy from a hot medium, usually steam.

EVAPORATOR 
Heat energy is transferred to a liquid until it evaporates (changes from liquid to gas).

FLOW PATH IN A SHELL AND TUBE HEAT EXCHANGER


The flow path of the fluids are fixed by the division plates in the heat exchanger heads for the cooling fluid and the internal baffles or tube support shets within the body of the heat exchanger for warm fluid:
The division plates in the heads or boxes fix the position of the inlet and outlet branches for the fluid passing through the tubes.

The internal baffles fix the position of the inlet and outlet branches for the fluid passing through the body of the heat exchanger on the outside of the tubes.

If the heat exchanger heads do not contain any division plates, he fluid passing through the tubes enters at one end of the heat exchanger and leaves at the other. This arrangement is referred to as a single pass heat exchanger. If the heat exchanger is a double pass type, a division plate is fitted in one head. The inlet and outlet connections for the fluid passing through the tubes are fitted on this head. The division plate prevents the fluid bypassing and causes it to pass through half the tubes in the heat exchanger which is referred to as the inlet bank. After the fluid passes through the inlet bank it enters the other head which is just a bobbin piece and a cover. The direction of fluid flow is reversed in this head or box and it passes back through the outlet bank of tubes and leaves at the outlet branch. The fluid has passed through the tubes in two different paths from which it gets the name two pass, or double pass.

In recent designs, the guided flow concept has been introduced, i.e. a secondary cooling surface in the form of radial fins integral with the tubes between which flow is guided radially, alternately out and in from section to section. This gives better heat transfer surface and better heat transfer, lower metal surface temperature and increase performance.

Baffles. They have thermal significance because the shell-side fluid is made to flow to and fro across the bundle from one end of the heat exchanger to the other. Another importance of baffles is that they are spaced to provide support to the tubes and prevent sagging of tubes and flow-induced vibration.

MATERIALS


Depending on the size and duty of the cooler the cylindrical shell may be of fabricated steel, cast iron or occasionally aluminium bronze. The tube plates are usually of Naval brass and the tubes of aluminium brass; occasionally 70/30 copper-nickel tubes are used. The usual method of securing the tubes to the tube plate is to roll-expand them. The cooler headers may be of cast iron. In such instances the headers act as sacrificial anodes, wasting in preference to the aluminum-brass tubes. Unless soft iron or mild steel sacrificial anodes or impressed current cathode protection is used to protect the cooler from corrosion such headers should not be painted internally.

Shell: Gun metal (copper, tin, zinc ); or cast iron.

Tubes: Aluminum brass (copper, zinc, aluminum) or cupro-nickel (copper, nickel)

Tube plates: Cast naval brass ( copper, zinc, tin ).
Arrangements for  Linear Expansion of Tube Stack.

There are three arrangements:

Ø One tube plate expands, shell and tubes fixed. In heat exchangers with cast bodies, one tube plate is fastened to the flange on one end of the body. The other tube plate is made to slide within the end of the body. Sealing is effected by fitting O-rings in circumferentially cut grooves. The O-rings contact the circular bored end in the body and the tube plate to make a seal. When there is a difference in expansion between the tubes and the body the differences are accommodated by the tube plate which slides relative to the body. With this arrangement the tubes can only be arranged for single or double pass flow. This arrangement is more commonly used for engine cooling water and lubricating oil coolers. It also has the advantage of allowing very easy removal of the tube stack from the exchanger body for chemical cleaning or repair. This is further facilitated if the cooler is mounted vertically and the sliding tube plate is at the lower end.

Ø Shell expands, tube plate and tubes fixed. In some types of heat exchangers the body is made of mild steel plates, and in order to cater for the differential expansion between the body and the tubes, a bellows ring is welded circumferentially a round the body of the heat exchanger. Differences in expansion are then catered for by the bellows ring that deforms slightly to accommodate the changing length of the tubes. This type of expansion arrangement can be used for any number of fluid passes through the tubes.The tube plates are bolted directly onto the flanges of the body and the tubes may be roller-expanded at both ends.

Ø Tubes expand, shell and tube plates fixed. A third arrangement is to fasten the tube plates to the shell of the exchanger and roller-expand and bell-mouth the inlet ends of the tubes. The outlet end of the tubes is fitted with a small stuffing box in the tube late and sealing is made by using cotton cord packing tightened by a threaded gland ferrule screwed into the threaded end of the stuffing boxes. Differences in expansion between the tubes and the exchanger body is accomodated by the tube ends sliding through the packing in the tube plate gland. This is a common arrangement for exhaust steam condensers.


Shell and tube geometric terminology
1
Stationary (Front) Head—Channel
   20
Slip-on Backing Flange
2
Stationary (Front) Head—Bonnet
   21
Floating Tubesheet Skirt
3
Stationary (Front) Head Flange
   22
Floating Tubesheet Skirt
4
Channel Cover
   23
Packing Box Flange
5
Stationary Head Nozzle
   24
Packing
6
Stationary Tubesheet
   25
Packing Follower Ring
7
Tubes
   26
Lantern Ring
8
Shell
   27
Tie Rods and Spacers
9
Shell Cover
   28
Transverse Baffles or Support Plates
10
Shell Flange—Stationary Head End
   29
Impingement Baffle or Plate
11
Shell Flange—Rear Head End
   30
Longitudinal Baffle
12
Shell Nozzle
   31
Pass Partition
13
Shell Cover Flange
   32
Vent Connection
14
Expansion Joint
   33
Drain Connection
15
Floating Tubesheet
   34
Instrument Connection
16
Floating Head Cover
   35
Support Saddle
17
Floating Head Flange
   36
Lifting Lug
18
Floating Head Backing Device
   37
Support Bracket
19
Split Shear Ring

SEPARATION OF THE FLUIDS
Arrangements to prevent the two mediums from mixing with each other consists of:

1.  Tubes expanded to the plates.

2.  Gasket between end box(header) and shell flange.

3.  O- rings between shell and free end of tube plate.

ARRANGEMENT FOR INDICATING LEAKAGE AT FREE END
Separation of the shell and tube fluids at the floating head is obtained by means of packing rings installed between the outside of the floating tube plate and recesses in the rear- head flanges. The shell and tube side fluids each have their own packing rings, which are separated by a lantern ring provided with weep holes for leak detection. Leakage at the packing will not cause mixing of the shell and tube side fluids within the exchanger itself.

The width of the machined bearing surface at the flating tube plate periphery must accommodate the two packing rings, the lantern ring and thermal movements of the bundle. In some cases the pressure of thickness of floating tube plate is sufficient, but if not, the extra bearing width is obtained by providing a machined skirt at the tube periphery. The skirt may be an integral part of the plate or attached by welding.

                
PLATE TYPE HEAT EXCHANGER 

The basic plate consists of a thin, rectangular, metal sheet into which a corrugated pattern has been formed by precision-pressing. One side of each plate has a full peripheral gasket. The complete unit comprises a number of such plates, mounted on a frame, and clamped together, face to face, by a bolting system. The pace between adjacent plates forms a flow channel and the system is arranged so hat the hot and cold fluids flow through alternate flow channels, parallel to the long side of the plates. Openings(ports) in the four corners of each plate direct the two fluids into their respective channels.

CONSTRUCTION

The most common metals use in plate type heat exchangers are titanium and stainless steel Others include titanium-palladium alloy and monel metal Carbon steel is rarely used because thin plates are required for pressing, which would have little corrosion resistance. Titanium provides very high resistance to corrosion by sea water.

PLATE CORRUGATION TYPES 

A wide range of corrugation types are available and the pattern and geometry are proprietary. The most widely used corrugated types are the inter-mating or washboard type, and the chevron or herringbone type. The plates are corrugated for two basic reasons:

1) Corrugations increase the effective area of the plate and promote turbulence. In he washboard type, turbulence is promoted by a continuously changing flow direction and velocity of the fluid. In the herringbone type adjacent plates are assembled such that the flow channel imparts a swirling motion to the fluid.

2) To enable such thin plates to withstand differential pressures up to at least 10 bar, and in special cases up to 25 bar, the corrugations are essential for strengthening and mutual support of the plates.

GASKETS
The periphery of each plate is grooved to house a molded gasket, which are usually cemented in; some are ‘snap-on’ type. The gasket is designed to provide a tight joint without local distortion of the thin plate. The integrity of the complete nit depends greatly on gasket performance.

Gasket materials range from nitrile rubber( maximum temperature of 135°C) to  Viton(175°C) and compressed asbestos fiber(260°C). Compressed asbestos fiber gaskets, however, are not widely used.

FRAME
The frame consists of a fixed head or fixed frame at one end, and a movable head or pressure plate at the other. The vertical sides of both the fixed frame and pressure plates are notched at intervals to engage tie bolts which join the heads together. The pack of plates are compressed together as the tie bolts are tightened at the movable head end. A horizontal carrier bar at the top of the frame, and a horizontal guide bar at the bottom, are attached to the fixed head plate at one end and an end support column at the other. Every heat transfer plate is free to slide along both bars. The movable head plate is similarly notched and free to slide along both bars. The frame is normally constructed in carbon steel.

PORTS
The fluids enter the unit via ports located in one or both end plates. If both inlet and outlet ports for both fluids are located in the fixed head end, then the unit may be opened up without disturbing the external piping. This applies to single-pass arrangements, but with multi-pass arrangements the ports must always be located on both heads. This means that the unit cannot be opened up without disturbing the external piping at the movable-head end.

The port entrance area is the weakest part of the plate because, unlike the peripheral gasket, the gasket in an adjacent plate is not supported by a corresponding one.

FLOW ARRANGEMENTS
Each traverse of either fluid from top to bottom of the pack, or vice-versa, is termed a pass. Usually, all passes have the same number of flow channels in each pass, but this is not always the case. Single- or multi- pass flow is possible.

LOOPED FLOW
A single pass by both fluids provides counter current or co-current and two arrangements, termed loop flow, are possible. In the preferred arrangement, all four ports will be on the fixed head-plate, with the advantage that the pack can be opened without disturbing any external piping.

ADVANTAGES OF PLATE COOLERS OVER TUBE COOLERS
1) Plate coolers are smaller and lighter than a tube cooler giving the same performance.

2) No extra space is needed for dismantling (a tube cooler requires enough clearance at one end to remove the tube nest).

3) Their higher efficiency is shown by the smaller size.

4) Plates can be added in pairs to increase capacity and similarly damaged plates are easily removed, if necessary without replacement.

5) Inspection and cleaning is simple as is maintenance.

6) Turbulent flow helps to reduce deposits which would interfere with heat flow.

7) With titanium plates virtually no corrosion or erosion would occur.

DISADVANTAGES OF PLATE COOLERS
1) In  comparison with tube coolers in which leakage tubes are easily located and plugged, leaks in plates are sometimes difficult to find because the plates cannot be pressurized and inspected with the same ease as the tube coolers.

2) Deterioration of joints are also a problem; they may be difficult to remove and there are sometimes problems with bonded new joints.
Tube coolers may be preferred for lubricating oil cooling because of the pressure differential.

3) Cost is another drawback; there are a large number of expensive joints on plate coolers and the plates are expensive.

VARIOUS TYPES OF HEAT EXCHANGERS IN USE ON SHIPS 
1.  Charge Air Coolers. These are finned-type tubular heat exchangers to provide for better heat transfer, since air is a poor conductor of heat.These coolers are normally rectangular in form.

2.  Electric Machine Coolers. Some large alternators and electric motors are designed for operation with closed ci5rcuit air cooling. Heat must be extracted from the circulating air and, for this purpose, finned tube units are employed, inserted into the air ducting. Sea-water flows through the tubes, while the air passes over them, flowing between the fins. Spray baffles are usually fitted to these units so that, in the event of puncture of one of the tubes, sea-water will not low directly into the alternator or motor.

3.  Oil Heaters. For burning heavy fuel oil in a boiler furnace, or a compression ignition engine, it is necessary to pre-heat it. Steam is used as the heating medium in fuel systems and lubrication systems. The type of heater used is multi-tubular; the tubes are bent into a U- shape and fitted with expanded ends into a single tube plate. The liquid head or box is fitted with a division plate in its middle so that the oil flow takes a two-pass flow. The oil enters the inlet branch of the liquid head, passes through one leg of the U, round the bend    and leaves by the other leg. The division plate separates the inlet and outlet legs of the U-shaped heater tubes. The inlet branch is always on the lower side. Tubes are sometimes fitted with fins bonded to them(the oil flowing outside the tubes) and tubes fitted internally to promote turbulence in the oil flowing through them.  
  
AIR PRE-HEATERS
The combustion air required for forced- draught boiler furnaces may be heated by the exhaust gas in order to improve the overall efficiency of the whole cycle. This may be carried out in a conventional heat exchanger, air passing outside the tubes and exhaust gas inside them.

SEA-WATER HEATERS
These are usually the shell-and-tube type construction, with a fully floating head. The sea water to be heated flows in several passes through the tubes, being heated by the condensation of steam in one part of the tube bundle and sub-cooling the condensate in another.

REFRIGERATION SYSTEM
Shell-and tube type condensers are used, sea water  circulating through the tubes and refrigerant condensing in the shell. External fins to improve heat transfer are sometimes used outside of the tubes.

CONDENSERS
A condenser is a vessel in which vapor is deprived of its latent heat of vaporization and so changed to its liquid state, usually by cooling at constant pressure. In a steam system, steam enters at an upper level, passes over rubes in which cold water circulates, falls as water to the bottom and is removed by a pump or flows to a feed tank. The tube arrangement provides for condensation with minimum loss of heat: the cooling water normally circulates in two passes, entering at the bottom.

CONTROL OF TEMPERATURE IN HEAT EXCHANGERS
There are three basic ways by which the temperature of the hot fluid being cooled in a heat exchanger may be controlled, when the cooling medium is sea water.
a)  By by-passing a proportion of the hot fluid flow, the remainder being passed through the heat exchanger.

b) By throttling the sea water flow, or, alternatively, by-passing a proportion of it.

c)  By controlling the temperature of the sea water entering the heat exchanger—this is done in the sea water system as a whole, by spilling part of the heated discharge back into the pump suction.


MAINTENANCE OF HEAT EXCHANGERS

The only attention that heat exchangers should require is to ensure that the heat transfer surfaces remain substantially clean and the flow passages generally clear of obstruction. Indication that undue fouling is occurring is given by a progressive increase in the temperature difference between the two fluids, over a period of time, usually accompanied by a noticeable rise in pressure loss at a given flow.

Fouling on the sea water side is the most usual cause of deterioration in performance. The method of cleaning the sea water side surfaces depends upon the type of heat exchanger. With the shell-and-tube type, the removal of the header covers or, in the case of smaller heat exchangers, the headers themselves, will provide access to the tubes. Obstructions, dirt, scale etc., can then be removed, using the tools provided by the manufacturer. Flushing through with fresh water is recommended before a heat exchanger is returned to service. In some applications, such as piston oil cooling, progressive fouling may take place on the outside of the tubes. Most manufacturers recommend a chemical flushing process to remove this in- situ, without dismantling the heat exchanger.

Plate heat exchangers may be cleaned by unclamping the stack of plates and mechanically cleaning the surface of each plate as recommended by the manufacturers. The plate seals may require replacement from time to time and here the manufacturers’ instructions should be closely followed.

Although maintenance is a rapid, simple operation, the heat transfer plates must be handled with care.

Corrosion by sea water may occasionally cause perforation of heat transfer surfaces. This will cause leakage of one fluid into the other but this is not always easy to detect whilst the leakage is small, although substantial leaks may become evident through rapid loss of lubricating oil, jacket water etc.
Location of a perforation is a straight forward matter in the case of a tubular heat exchanger, whether this is of the shell-and-tube type or of other tubular construction. Having drained the heat exchanger of sea water and removed the covers or headers to expose the tube ends, some flow of the liquid on the other side of the surface will be apparent, in the case of oil and water coolers, from any tubes which are perforated. To test for leaks in air coolers drain coolers etc. each tube in turn can be plugged at each end and pressurized with air; inability to hold pressure indicates a leak.

To aid the detection of leaks in a large cooler such as a main condenser, in which it is difficult to get the tubes dry enough to witness any seepage, it is usual to add a special fluorescent dye to the shell side of the cooler. When a ultra-violet light is shone on to the tubes and tube plates any seepage is seen since the dye glows with a vivid green light. In plate heat exchangers, the only way to locate leaks is by visual inspection of the plate surfaces.

On docking for any protracted period, such as for repairs, refitting etc. it is advisable to drain the sea water side of heat exchangers, clean and flush through with fresh water, after which the heat exchanger should be left drained, if possible until the ship re-enters service. 
Wednesday, August 21, 2013
Posted by Unknown

SEAFARERS 'BILL OF RIGHT' IN FORCE TODAY


Tuesday 20,  August 2013
The date when the Maritime Labour Convention (MLC) 2006, comes into force for ships flagged in those states that signed up to it exactly one year ago.
More states have since signed the convention, and the MLC will take effect for them one year on from the date they signed. Currently, 47 member states of the International Labour Organization (ILO) have signed up to the MLC, representing more than 75 percent of the world’s gross tonnage of ships.


The MLC sets out seafarers' rights covering:    •    minimum age 
•    employment agreements 
•    hours of work or rest
•    payment of wages 
•    paid annual leave 
•    repatriation at the end of contract
•    onboard medical care
•    the use of licensed private recruitment and placement services  
•    accommodation   
•    food and catering  
•    health and safety protection, and accident prevention
, seafarers’ complaint handling.
The ILO has issued a useful background guide to the MLC and what it means. This can be found at: http://www.ilo.org/global/standards/maritime-labour-convention/news/WCMS_219628/lang--en/index.htm
Tuesday, August 20, 2013
Posted by Unknown

STARTED CAREER AS ORDINARY SEAMAN(O.S)

If you’re just staring out on the maritime industry, this is the bottom rung on the ladder. In families long in boating tradition, children usually start in this job and work their way up to becoming the owner of the ship.

He is one of the unlicensed members of the deck department and the main duty is maintaining the cleanliness of the whole ship.Being an ordinary seaman is an apprenticeship for one to be promoted as able seaman. An ordinary seaman should work for a specific period referred to as “sea time” before he will be allowed to take certain courses and trainings to gain a higher rank.


Basic Tasks
The Ordinary Seaman performs any of the tasks below:
Paints, buff and scales decks and ship’s structure. The metal properties of the ship is always at risk of developing rust and being damaged because of constant contact with sea water. The Ordinary seaman needs to spend a lot of time removing rust and fixing damages of affected areas by using paints, sealants and primers.
Ensures that the ship’s deck is free of water and dirt. The ship’s deck is often filled with sea water which is a hazard because the water and salt can make the floor dirty and slippery. The sea water also cause the deck to accumulate rust faster and can damage the ship’s equipments. Sweeping and washing the deck is one of the many duties of the OS.
Splice and knot wire and rope. The skill of tying the knot is one of the most identified skills of an Able Seaman. As being an OS is an apprenticeship, he is asked to demonstrate his knowledge of knot tying under the auspices of senior members of the deck department.
Loads and Unloads Cargos.  The job of an ordinary seaman involves moving heavy cargos and large equipments. The types of cargos and equipments that an OS needs to load and unload depend on the type of ship.
Protects Cargo. When a cargo is brought to the ship, the OS is in charged of securing or fastening it to ensure that it will not be damaged by the constant movement of the vessel. The process of doing this varies depending on the kind of ship.
Boat launching and boat recovery. An OS is usually given lifeboats drills to be trained in launching, navigating and retrieving lifeboats. This routine is required in all merchant ships by International Regulations.
Posted by Unknown

TYPES AND DESCRIPTION OF CRUISE LINE JOBS



A cruise ship can be floating and cruising in the water for days and weeks carrying passengers that are out for a good time. But what makes a cruise successful for these passengers? Is it the good facilities? The good sites? The cruise pleasure and experience? Or the people working to give the best service in a cruise ship?

All of these are considered in what we can call a good cruise along with the people that are in the ship. A ship can also be considered as a small city as a community is formed with in it. Strangers become friends, crews and clients interact and workers becomes tourists. Yes, workers on a cruise doesn't just work all the time, they do enjoy and have fun as well as they are a part of that community. You too can be a part of the community wherein you are paid to travel. To give you a general idea of the types of cruise ship careers at cruise lines, here are a few detailed job description, qualifications and duties:

Cruise Ship Entertainment Jobs


Almost always synonymous with “cruise staff”, these positions are considered most glamorous jobs on the ship and are the most in demand career. Cruise ship entertainment jobs deals with anything relating to passengers entertainment. This may include hosts and hostesses, cruise director jobs and staff, performers, disc jockeys, cruise ship musician, shore excursion staff and swimming instructors.

Cruise Ship Deck and Engineering Jobs

Responsible for maintaining and running the vessel, this department doesn’t usually accept entry-level positions and mostly only experienced merchant marines that include maintenance workers, deckhands, engineers and ship officers who are in charge of passenger safety. It is their task to sail the ship, maintain the ship performance and physical state and keep it in accordance with fleet regulations and international maritime laws.

Cruise Ship Service Jobs

Jobs on this department are concerned with managing the restaurants, bars and passenger cabins, as well as shipboard retail concessions like souvenir and gift shops. They are the ones who serves food, beverages or any kind of product that can generate them a good amount of tip from the passenger. The ship’s treasurer in charge of passenger accounts, currency exchange, ticketing and more, also called the purser, are also included in this category.

Cruise Ship Personal Care/Service Jobs

Fitness, beauty, spa and medical services are included in this category. This are very important jobs in a cruise ship since most passengers signed up for a cruise to enjoy themselves, relax, be comfortable and pamper themselves and the medical department are to render services in times of medical emergencies like simple cuts and bruises, allergies and being sea sick.

Cruise Ship Office Jobs

Office positions are generally for employees who works in the main office or branch arranging cruises, managing accounts or performing general office work onshore. Positions like administrative assistants, sales/marketing staff, clerical workers and booking agents are some of the jobs available in this category.

Different cruise lines uses different categories or department for the cruise jobs that are needed in their ships but the listed jobs above are the most used categories.
Posted by Unknown

Recent

SANJAY SWAIN. Powered by Blogger.

- Copyright © MARINE EBOOKS -Metrominimalist- Powered by Blogger - Designed by Johanes Djogan -