Working Principle of Fresh Water Generator on Board Ship

Working Principle of Fresh Water Generator on Board Ship

Fresh water generator(FWG) is one of the essential machineries on board ship, After-all a large amount of fresh water is utilized on ship every day. On board ship Fresh water is used for the most part by huge boilers having steam turbines as main propulsion or cargo pumps driven by turbines. They all in all record for 30+ Tons of fresh water every day separated from the day by day necessities of 10+ ton for crew consumption as drinking, cooking, washing,Tank cleaning and different utilities. Adequate consumable water might be taken up against the cargo load capacity in the port for satisfying crew and machinery necessity yet isn't prescribed to utilize shore water for boilers because of their low quality, so Fresh water generator is unavoidable on board ship.

But why do we need the FWG on board in first place?

In the middle of good old days people used to bring across lots of water in their ship. It was good however it expands the load on the ship and furthermore water lack issues were always there. Be that as it may, the nature of shore water will be extremely (too much) bad to be used in water tube boiler and filling (expansion) tanks. The storage space that could have been used for fresh water can as a result be used for fuel or added/more space for payload and products (that are bought and sold) when fresh water generator is installed on a ship. As you may know the first (or most important) concern for running a ship or any transportation business is to make money. Further more Boiler needs demineralized water to reduce overall scale development and corrosion issues. It is also normally used to build the general efficiency of the running machinery, mostly it uses the engine warmth/heat by Cooling The Hot Jacket Cooling Water At Around 85 Deg Celsius To 65 Deg Celsius.

Working Principal Of FWG?


Extremely important rule of all low weight freshwater generator is that, boiling point of water can be decreased by lessening the pressure of the air surrounding it. By keeping up a low pressure, water can be bubbled at low temperatures say 55 degree Celsius. The source of warmth for the fresh water generator could be waste heat rejected by generators and main engine jacket cooling water. This decrease In Saturation Temp lead to early vaporisation of water due to vacuum created within the chamber. It Is Created By The Help Of An Air Ejector, Which Extracts The Air From That compartment/chamber. An Air Ejector Works On Bernoulli's Rule and being used side by side with a brine ejector used to suck salt water from the chamber. The vacuum help disappear the water leaving behind the salt or salt water to be sucked by salt water ejector. It is then passed through the dimmister (A sort of punctured plate with very minute gaps) which traps any water or salt particle traveling through it. The evaporated water is then condensed together with the help of ocean water and after that tested for sality with the help of salino-meter.


Regulations Regarding Production of sea water on board ship:


  1. Ship must be 12 nautical miles away from the nearest coastline to start the FWG.
  2. Engine must be running at full ahead sea speed during start of FWG.
  3. Ensure main engine parameters are normal.
  4. Ship is not in congested water.
  5. Ship is not maneuvering.
  6. There is no oil/chemical spill reported in the visinity of the ship.

Safety Equipments on A Typical FWG:

1. Vacuum Breaker For Releasing Vacuum when we shut down the FWG.

2. Relief Valve For Releasing The Excess Pressure.

3. High Salinity Alarm: It Is Fitted To The Salinometer As It Measures Higher Salt Content In The Water Produced.

4. Temperature Gauge.

Starting Procedures for Fresh water generator:


  • First we need to ensure that suction, discharge and overboard valves for ejector pumps are under open condition. Now once been checked, start the ejector pump.
  • Close the vacuum breaker valve.
  • Make Sure the S.W pressure at ejector (air) is not less than 3 bar. Now wait for 10-15 minutes to build vacuum in the generation chamber of fresh water generator. Wait until it shows more than 90% vacuum.
  • Now open the sea water feed to the evaporator. Check for the sea water level in the shell through the sight glass and ensure it is at optimum level controlling feed through feed valve. Once the heating coils are fully submerged by the sea water open the J.C.W valves to the evaporator slowly.
  • Purge out any air in the system by opening air vent at the top of the evaporator.
  • Check for evaporation from the sight glass and then start the salinometer.
  • Divert the outlet back to the feed water until the salinity is under the limit.
  • When the salinity level is as per the desired or set value, open the discharge valve of distillate pump which sends the water to the fresh water holding tank through flow meter.
  • Increase the evaporation rate and start the discharge pump. Check for the sytem to be stable.



Author Amit                                                          Article requested by: NIÑO GONZALES


Ship side valve Functions, Definitions and Specification


The valves on the side of the ship / Ship-side valves on the top refer to valves that are connected to the hull, without having anything to medium with the valve on the side of the ship. During the dry dock, the valves are checked by the dry dock personnel, while the work of the ship's engineers is to check the internal valves. For total seaworthiness of the ship, the ship side valves must always be in proper condition, They must have local as well as remote control operation which must be permanently connected. Pipes of the inlet and the outlet to the sea must be provided with valves or taps attached directly to the outer coating or to the plating’s of fabricated water boxes attached to the shell plating. These accessories must be fixed with threaded bolts equipped with hazelnuts.
Heads or bolts screwed into heavy steel pads built into the plating. Screw holes must not penetrate into the plating. Valves for the Ship side Side Applications must be installed so that the pipe section can be located directly inside the valve without removing the sealed integrity of the hull. Taps and accessories of the ship, when made of steel or other approved material with low resistance to corrosion, must be adequately protected against wastage/rusting. In the visual inspection, the valves should not show any sign of defects on their body, their internals and the spindle. The Thread and other parts must be in good condition, which ensures freedom of movement in the operating conditions. Ship side valves are made and tested in accordance with the rules and regulations of the classification society in the presence of an expert.


Markings on the Ship Side valve of the Ship: The following data are marked on each side of the valve.

a) Nominal size of the drill (eg NB 80);
(b)Nominal pressure according to section 1.4.
c) Test pressure
d) Brand / seal of the manufacturer.
e) Marker / Stamp of Classification Surveyor.
f) Flow direction
g) The weight of the valve to be marked.
h) Metallic tag numbers provided with the table.

Why are they so important?

In a Ship, all that has been installed has a purpose, besides the valves on the side of the ship is controlled and supervised by the classification society. Maritime organizations (classification society and flag state) know a series of incidents of local flooding machinery space installations and averaging two reports of floods received annually. The side flaps ensure the sealed integrity of the shell and the internal working sea tube from the sea. Operation of the valves allows maintenance of pipeline equipment. They are used to prevent the ingress of water into the compartments after a failure in a pipeline or equipment. Therefore, the valves must provide a watertight barrier when closed. In normal commercial vessels, the ship is docked dry and the ship's valves are inspected to meet classification society standards. This inspection confirms the condition of the valve and closes it when closed. For installations, such as mobile drilling units of fleets or ships of intervention, the inspection may be performed by dry dock times or repair in the port, however, permanently anchored facilities these inspections are carried out. They become more complicated as the right holder must be able to demonstrate that the valve is sufficiently leak-proof and in good condition. This can be combined by a close visual inspection and on-site testing. After repairing or installing a new valve, the dry dock repair shop usually provides a 5-year warranty on these valves. However, if the valves are damaged during the warranty period, the workshop will bear the cost of the diver's time and expenses.

Listed below are few Ship-side valves that is seen on vessels.

              Name of the Valve                                Side                          Type                        Specification

1  Sea water suction for low sea chest                   Starboard      Butterfly valve           10K 550A
2  Sea water suction for high sea chest                  Port               Butterfly valve           10K 550A         
3  Sea water suction F.W.G sea chest                     Starboard      Butterfly valve           10K 125A         
4  Main cooling S.W discharge overboard             Port               Butterfly valve           10K 300A               
5  O.W.S discharge overboard                                Port              SDNR                         10K 40A          
6  Fire & G.S pump discharge overboard               Starboard     SDNR                         10K 200A             
   (fire and ballast pump)                                                             (Screw Down Non-Return valve) 
7  Steam blow valve to high sea chest                    Port              SDNR                         16K 40A            
7a Air vent for high sea chest                                 Port              Ordinary Globe valve(SDGV)   10K 40A                         
8  Steam blow valve to low sea chest                     Starboard     SDNR                         16K 40A           
8a Air vent for low sea chest                                  Starboard     SDGV                         10K 40A              
9  Steam blow valve F.W.G sea chest                     Starboard     SDNR                         16K 40A      
9a Air vent for F.W.G sea chest                              Starboard     SDGV                         10K 40A                     
10 F.W.G discharge overboard                                Port             Butterfly valve            10K 125A                         
11 Boiler blow down direct overboard                    Port            SDNR                          16K 40A               
12 Soil/waste water discharge overboard                Starboard   Storm valve                  10K 100A                         
13 Stop valve for waste water overboard                Port            Storm valve                  10K 100A                  
14 Gally/provision refer drain overboard                Starboard   Storm valve                  10K 100A                       
15 I.G system scrubber cooling tower                     Starboard   Butterfly valve             10K 200A                             
   discharge overboard 
16 Draught gauge overboard valve                          Starboard   SDGV                         10K 50A                      
17 Weather deck scupper overboard                        Port                                                125A  
18 Weather deck scupper overboard                        Starboard                                       125A  
19 Main water ballast pump discharge overboard   Port            Butterfly valve            10K 550A             
20 ODME discharge overboard                               Starboard   Butterfly valve            10K 350A    

What does K and  A stand for in specifications?

 K : is the pressure.
 A : is the Nominal diameter of the pipeline.  


*Note: The Following Article is being Originally written by one of our co-Author (Arpit Singh) on his personal website and is being re-used with proper modifications, editing and due permission. If you have any problem with any part of the content please contact us, We will act ASAP.



Author ARPIT SINGH and Amit


How inert gas is produced on board ship?

How inert gas is produced on board ship?

The Inert gas is produced in the IGG by the combustion of fuel with air. Marine diesel oil (MDO) or MGO is drawn from the storage tank and pumped through a filter to the main burners. A blower delivers the air necessary for combustion.
Oil and air is mixed in the correct proportion in an air-atomizing burner, which is ignited by the pilot burner. The fuel-air ratio and the oxygen content of the IG can be regulated by a valve in the fuel supply line to the main burner. Purple-blue to rose-purple flame indicates good combustion whereas yellow flame means too much fuel oil or too low delivery air pressure causing low atomizing pressure and risk of soot formation.

The inert gas thus generated consists of mainly Nitrogen and carbon dioxide. It is first cooled in the combustion chamber by means of a sea water jacket, which surrounds the combustion chamber. The gas then comes in direct contact with a water spray. The resultant IG comprises of:

Oxygen  :            2% by volume
Carbon dioxide: 13% by volume
Nitrogen   :        85% by volume

Due to perfect combustion, there is a complete absence of soot. The temperature of the gas leaving the generator is about 5-10* above the cooling water temperature.
During the operation, should there be a reduction in demand for the IG, the excess gas is vented to the atmosphere. The operation is continuously monitored for flame, water or control air failure and excessive cooling water level. Should any emergency condition arise, the IGG automatically shuts off and sounds an audible alarm.
This is a costly installation, which is usually found in product or chemical tanker. With some clean cargo tainting could be a problem, if flue gas from boiler is used.

Chemical tankers & Product tankers are normally FRAMO tankers hence IGG is fitted on these ships, secondly the quality of IG plays a very important role in maintaining the quality of chemicals being transported.
Conventional tankers with turbine driven COP will always have a large water tube boiler and thus Inert gas on these ships will be produced from boiler flue gas. Boiler will be used continuously during cargo discharge for running the cargo oil pump turbines (COPT).
On Framo tankers, the cargo discharge system consists of each cargo tank having a fixed submersible cargo pump, this pump is coupled to a hydraulic motor. The hydraulic motor is driven by high pressure hydraulic oil (220 bar), this high pressure hydraulic oil is delivered by hydraulic power-packs located in the engine room, these power packs are normally driven by diesel engines. Thus these ships use an IGG for production of inert gas. They do not have large boilers as no turbines are present, hence IG from boiler uptake is not possible.
Carbon Molecular Sieve type Nitrogen Generator

The molecular sieve nitrogen generating plant is usually installed on ships such as chemical carriers where oxygen critical cargoes may be carried and purity of the inert gas is of utmost importance.
The system uses the pressure swing absorption method using a carbon molecular sieve which has the unique property of absorbing oxygen in preference to and at a faster rate than nitrogen. When air passes through the molecular sieve, oxygen is absorbed. Nitrogen gets across and is collected. However the sieve gets saturated with oxygen after sometime and needs to be changed over.
The system uses two vessels packed with the carbon molecular sieve. The vessels are alternatively on line or in the process of regeneration. As one reaches saturation, the system switches to the second. Change over time is appox. 1 minute.

The oxygen from the saturated sieve is removed by applying a reduced pressure to the vessel and then venting to the atmosphere. The nitrogen gas thus generated is fed to a buffer vessel from where it is distributed to the inert gas line. The purity of the nitrogen depends on the flow rate and can be as high as 99.5%. The lower the flow rate, the higher the purity and vice versa.

Image credit: Ankit Raj (Facebook)
*Note: The cover image is taken from the facebook page of "Ankit raj" after taking his permission, if anyone has any problem with the picture, please contact us we will act ASAP!


Author ARPIT SINGH

How to apply for marine engineering | Admission


A Naval/Marine engineer has too many tasks and duties to take over. A marine engineer has all the functions and marine engines to check. In short, a naval engineer is a person who deals with everything related to the ship, from small things to big issues. Now the responsibility of ship engineers is not only related to ships, but also must ensure the safety of the crew and sailors.

Being A marine engineer is a lucrative job offer. A marine engineer acquires considerable knowledge and the ability to work under pressure and difficult conditions at sea. They are the true saints with jack of all trades and an ace of diesel engines. Working in  the transport company makes them meet and see many universal things as well as exposure to the outside world. They know how the configurations of the nations of the world are the same. They know how to get at different places in the world "Things Done". They look like the experts end their work quietly making the wheels of the global economic race.  


About the course: -

Marine Engineering is a 4 year regular course in various colleges in India specially situated in coastal areas. For four years of maritime engineering, B.Tech has been a course of proficiency in naval/Marine engineer officer class IV, issued by the Directorate-General for Shipping, Government of India, after six months of maritime service, the cadets will sail marine engineers worldwide on board Trade. This course is strictly residential.


Eligibility criteria to apply for marine engineering:

The Eligibility criteria for admission to B.Tech (Marine Engineering) :

Academic Qualifications: The candidate must have successfully completed the Senior Secondary Examination (10+2) or its equivalent with :
i)  At least 60% marks in Physics, Chemistry and Mathematics (PCM) and
ii) At least 50% marks in English either in Class X or Class XII.

Age: Candidates  less than 25 years of age as on 1st of August in the year of admission will be eligible to apply. The date of birth as recorded on the applicants School Leaving Certificate will be considered for this purpose.
* The Upper age limit for admission relaxed for SC/ST candidates by 5 Years.

Marital Status: Only Unmarried candidates will be considered.
Physical and Medical Standards : Medically fit as per the standards set by Merchant Shipping Medical Examination Rules, 2000 as
amended from time to time.

Eye-sight :
Distance vision (unaided) 0.5 (values given in Snellen Decimal Notation) (6/12) in each eye or 0.67 (values given in Snellen Decimal Notation). (6/9) in better eye and 0.33 (Values given in Snellen Decimal Notation) and (6/18) in other eye. Normal colour vision.
Admission Procedure:
Through online / off-line examination, Interviews, Psychometric Test, And Medical Test.
The Entrance test format is multiple choice type. Candidates can be asked questions related to their 10-12th education, general English, etc. Selected applicants will be invited to a personal interview and later to psychometric test to assess their psychology including their suitability for a career In the sea. The selected candidates will be sent for medical examination. The final selection is obtained based on the ratio after the medical examination.


Some best Marine Engineering Colleges in the Country:

India is home to some of the oldest and at the same time the best institutes for studying nautical architecture, Marine engineering and science. Affiliates to the respective universities, colleges and courses, which are approved by the National Accreditation Board (NBA) and the Technical Education Council of India (AICTE).

A few of the best are:
  1. Tolani Maritime Institute (TMI),Mumbai.
  2. International Maritime Institute, Noida.
  3. Vels Academy of Maritime studies, Chennai.
  4. Maharashtra Academy of Naval Education and Training (MANET), Pune.
  5. International Maritime Institute (IMI), Delhi.
  6. International Maritime Academy (IMA), Chennai.
  7. Institute of Technology and Marine Engineering (ITME), Kolkata.
  8. Coimbatore Marine College (CMC).
  9. Samundra Institute of Marine studies, Mumbai.
  10. Academy of Maritime Education and Training (AMET).
Other best international college:

Hard to get a job as TME or Deck Cadet ? | Getting started on job hunt


For the past few years, I have been noticing how difficult it has been to get a job as trainee marine engineer or deck cadet on ship after completing marine engineering or nautical science course even from a well recognised maritime institute. The main reason behind this would be the approval of so many substandard institutions by the government in recent years, because of which the number of students graduating every year is far more than the number of job openings that we have. Along with this, a lot of job agents, mostly fraud ones have come up offering jobs in known and unknown companies taking a huge amount of money and you would wonder that the average agent fee they are charging has been above 3.5 to 4 lakh INR for a normal company and 5 to 6 lakh INR for a well known highly paying company which is one third of actual engineering course fee itself. The funniest part in fact is that the agents get only 10 to 15 % of the fee and the rest goes to the people who are sitting on top of crewing department in these companies, even the best shipping companies I would say.Though it is rare that the companies take freshers from outside without reference, there are few companies that do recruit cadets on regular or non-regular basis. Some of them are below.

1. Shipping Corporation of India, SCI ( www.shipindia.com )

2. Wallem Ship management ( www.wallem.com )

3. Nortrans Maritime ( www.nortrans.com )

4. United Ocean Ship management ( www.uosm.com )

5. Seastar Ship management ( https://www.seastargrp.com/shipping )

6. V-Ships ( www.vships.com )

Links of mumbai located companies are below ( in case if you guys want to do job hunt ).

Shipping Companies in Andheri West - https://www.justdial.com/Mumbai/Shipping-Companies-in-Andheri-West/nct-10432101

Shipping Companies in Andheri East -
https://www.justdial.com/Mumbai/Shipping-Companies-in-Andheri-East/nct-10432101

Shipping Companies in Nariman Point -
https://www.justdial.com/Mumbai/Shipping-Companies-in-Nariman-Point/nct-10432101

Shipping Companies in CBD Belapur -
https://www.justdial.com/Mumbai/Shipping-Companies-in-Cbd-Belapur/nct-10432101

I wouldn't say not to approach agents for a job because the fact is that 70% percentage of the students graduating from most of the maritime colleges don't get their placement and to get one, they should either have very good contacts in shipping or they should look for a genuine agent. Over the years, I have seen many trainee engineers and deck cadets coming to mumbai to find an agent, some of them get a job after long waiting, some of them don't and the rest of them get cheated by fraud recruiters. If you are a fresher and you are paying money to an agent, make sure the company they recruit you to is approved by DG Shipping of India and has an RPSL ( Recruitment & Placement Services License ) number which is not expired. 

Never ever pay the agent before your contract letter is signed !!!!

Use the link below to see DG Shipping approved manning companies in India -

http://www.dgshipping.gov.in/Content/RPSAgencies.aspx

I wish Indian government would take some actions against..........

To read the full article click here



Guest Author Name: Jishnu Varakoth
Social Profiles: ?
Website link: 

2. http://marinejobsforfresher.blogspot.in

Short Bio: Marine engineer with good sailing experience. He is also a blogger and writer.

Post Source: http://traineemarineengineer.blogspot.in/2017/07/vacancy-for-trainee-marine-engineers.html

* The following article is originally written by the guest author and is partly produced as it is taken from original source for the help of maritime society with better understanding the new challenges. Proper permission is being taken from guest author prior to using the post and all care is being taken to avoid copyright issues but in no cases the blog owner or other permanent authors are responsible for any copyright claims. Inform us if you have any problem with the content.

General arrangement of IG Plant, Production and Deck Distribution System


General arrangement of IG Plant, Production and Deck Distribution System
The 3 elements necessary for combustion are : 1. Fuel(hydrocarbon vapour),  2.Heat(Source of Ignition),  3.Air(Oxygen); Oil tanker is basically meant for carriage of petroleum products/crude oil, thus fuel is available in plenty on board. Heat includes various sources of Ignition; these are also plenty on board from boilers, generators, hot work, galley, smoking etc. Air is present all around us, thus all 3 sides of the fire triangle exist on board a tanker, and therefore the flammability hazard is always present.

Why IG is required?

To maintain a safe atmosphere within ship’s cargo tanks a fixed inert gas system is used. Hydrocarbon gas normally encountered in petroleum tankers cannot burn in an atmosphere containing less than approximately 11% oxygen by volume. Accordingly, one way to provide protection against fire or explosion in the vapour space of cargo tanks is to keep the oxygen level below that figure. This is usually achieved by using a fixed piping arrangement to blow inert gas into each cargo tank in order to reduce the air content, and hence the oxygen content, and render the tank atmosphere non-flammable. As inert gas is added to the hydrocarbon gas/air mixture, the flammable range decreases until a point, is reached where the LFL and UFL coincide. This point corresponds to an oxygen content of approximately 11%. No hydrocarbon gas/air mixture can burn at this oxygen level. For practical purposes and to allow a safety margin, 8% is taken as the level of oxygen at which no hydrocarbon gas/air mixture can burn under any circumstances. To prevent fire or explosion in a tank containing a hydrocarbon gas/air mixture, it is therefore necessary to produce and supply inert gas having an oxygen content not normally exceeding 5% and to displace the existing air in the tank until the resultant oxygen level throughout the tank does not exceed 8% by volume.

Inert gas systems should be capable of delivering inert gas with an oxygen content in the inert gas main of not more than 5% by volume at any required rate of flow; and of maintaining a positive pressure in the cargo tanks at all times with an atmosphere having an oxygen content of not more than 8% by volume except when it is necessary for the tank to be gas free. 

Lower flammable limit (LFL): It is the concentration of a hydrocarbon gas in air below which there is insufficient hydrocarbon gas to support combustion. It is also referred to as Lower explosive limit (LEL). Mixture below this limit is also called as lean mixture.

Upper flammable limit (UFL): It is the concentration of hydrocarbon gas in air above which there is insufficient amount of air to support and propagate combustion. It is also referred to as Upper explosive limit (UEL). Mixture above this limit is called as rich mixture

Sources of inert gas; Possible sources of inert gas on tankers are:

1. Uptake gas from the ships main and auxiliary boilers.
2. An independent inert gas generator.
3. A gas turbine plant when equipped with an afterburner.
When an independent inert gas generator or a gas turbine plant with afterburner is fitted, the oxygen content can be automatically controlled within finer limits, usually within the range 1.5% to 2.5% by volume, and not normally exceeding 5%.

In certain ports, the maximum oxygen content of inert gas in the cargo tanks may be set at 5% to meet particular safety requirements, such as the operation of a vapour emission control system. Where such a limitation is in place, the vessel is usually advised of the requirements in the pre-arrival information exchange.

The Inert gas, besides not supporting combustion, should also fulfill certain other requirements, such as –
1. It should be non-reactive with cargo (e.g. in case of chemical gas)
2. It should not taint cargo (e.g. product)
3. It should not react with tank material (e.g. not causing corrosion)
4. It should have negligible or no toxic constituents.
5. It should be easily available at reasonable cost.

Other advantages of using IG are:

1. Positive pressure is maintained in the tank. This keeps out other gases that could cause combustion.
2. The positive pressure helps a faster discharge rate.
3. It prevents cargo loss due to evaporation.
Oil tankers may be fitted with an IG system, which utilizes the flue gases from engine room boilers as a means of reducing the oxygen content in cargo tanks. Some vessels may be fitted with IG Generators which are self contained units burning diesel oil to produce inert gas.

Usually, the inert gas composition is:

Oxygen (02) % by volume:  2 to 4%
Carbon dioxide (CO2) % by volume :  12 to 14%
Nitrogen (N2) : Balance
Sulphur dioxide (SO2) : Traces
Carbon monoxide (CO) : Trace
Nitrogen Oxide (NOX) : Trace
Water vapour H2O : Trace (high if not dried)
Ash and soot (C) : Traces

GENERAL ARRANGEMENT OF THE INERT GAS SYSTEM.

 GENERAL ARRANGEMENT OF THE INERT GAS SYSTEM.

Flue gas generated from the boiler flows through the Boiler Up-take Valve and into the Scrubber. There, the gas is cooled down and washed by sea water supplied by the Scrubber Water Pump. Before leaving the Scrubber the gas passes through the Demister where water droplets are removed before entering the Blower suction. On the discharge side of the Blower, oxygen content and temperature of the flue gas are monitored. High oxygen content and high temperature activate alarms.

Inert Gas from the blower flows in to the Deck Seal through Inert Gas Pressure Regulating Valve. Main line pressure is automatically controlled to keep desired pressure constant. Excessive pressure is avoided by the Inert Gas Pressure Regulating Valve working in conjunction with the Recirculation Valve.
The Deck Seal isolates the boiler up-take from the deck line by using sea water and to prevent the backflow of the hydrocarbon gas. Inert Gas from the deck seal flows into the deck supply line through the Non-return Valve and Deck Isolating Valve and then enters each tank through the Inert Gas Supply Valve (some vessels do not have individual valves). The Inert Gas System can also be used for Gas Freeing by opening the Fresh Air Inlet Valve.

The P/V breaker is installed to protect the cargo tanks from excessive pressure or vacuum.

Functions of the Inert Gas System Unit

BOILER UP-TAKE VALVE
Flue Gas generated by the boiler flows into the Scrubber Unit through the Up-Take valve. This valve is opened by remote control on Blower start up and when the Blower stops this valve has to be closed in order to avoid Flue Gas entering the Scrubber Unit.
SCRUBBER UNIT
This is installed to clean and cool the flue gas and to reduce the sulfur dioxide (SO2 ) from the flue gas.
DEMISTER
The demister is provided to remove water droplets contained in the inert gas which have passed through the scrubber. Since the inert gas is cooled and cleaned at the scrubber, the gas at the scrubber outlet inevitably contains water droplets as a result of its direct contact with the sea water used for cleaning it and could thus overload the blower and damage and increase corrosion on the blower impellers.
BLOWER
Total blower capacity is more than 125% of total cargo pumps capacity. And combination of two blowers is;-two blowers together giving 125% (i.e. 62.5% each) of total cargo pump capacity. Thus two blowers must be used during normal cargo discharging one blower having 125% capacity plus one standby/ auxiliary with either 30/ 60/ 125% of total cargo pump capacity
RECIRCULATION LINE
This allows the blower to operate when the pressure regulating valve is being closed. Gas flows back through this line to the Scrubber and thus avoids pressure built up on the discharge side of the blower.
DECK SEAL UNIT
The IGS connects the boiler up-take indirectly with the cargo oil tanks, and while the system is not in operation, the backflow of the oil vapour under pressure from the cargo tanks must be protected against. The Deck Seal is provided for this purpose.
DECK ISOLATING VALVE.
The inert gas coming out of the deck seal unit is distributed to each cargo tank through this valve.
P/V (Pressure Vacuum)
BREAKER
Under normal conditions, the Breather Valve controls the cargo tank pressure/vacuum automatically when the I.G.S. is off. As a back-up safety device, a Pressure/Vacuum Breaker is fitted to the deck main piping and is designed to release pressure from this piping and cargo tanks to atmosphere in the event that the Breather Valve capacity is exceeded while operating the I.G.S.The P/V Breaker does not have any moving parts and is filled to be required level by oil or fresh water containing an antifreeze solution.

Inert Gas system is required under SOLAS Regulation 60 of chapter II-2, for all Petroleum tankers of 20000 dwt and above, keel laid after 1984.
Exhaust from Main Engine is not used for inert gas for 2 reasons:
1. Inert gas is most required during discharge in port, when the main engine is not running.
2. To ensure complete combustion of fuel, extra air is fed into the engine (turbocharged) resulting in greater concentration of oxygen in the exhaust.
3. Air fuel ratio cannot be controlled for getting a certain O2% in exhaust.

# Various books, study material and other online sources has been refereed prior to writing this article but no part is copied or produced  from any of the source but explained same thing in better detailed way.

Author: Amit                                                                                      

If you have any complain regarding the post please do contact us!

Refrigeration, Air conditioning system and ventilation

Refrigeration: is a process in which the temperature of a space or its contents is reduced to below that of surroundings.

Uses of Refrigeration:
1. Domestic fridge rooms on ships for preserving foodstuffs for the crew.
2. Accommodation air-conditioning system.
3. Reefer control air dryers in engine room.
4. Refrigeration is used in the carriage of some liquefied gases like LPG and LNG.
5. Reefer containers for carrying food stuffs.
6. Reefer ships where the entire cargo space is refrigerated for carriage of perishable fruits and meat products.
7. To cool bulk CO2 for firefighting systems.

Live & Dead Cargoes: The perishable foodstuffs carried as refrigerated cargo or as stores on ships can be categorized as dead produce such as meat and fish or as live produce such as fruit and vegetables.

Fruit and vegetables are regarded as live cargoes until consumed, because they continue to ripen though slowly under refrigerated conditions. Fruit and vegetables continue a separate existence during which oxygen is absorbed and CO2 is given off, with the generation of heat.

The purpose of refrigeration in the carriage of perishable foodstuffs is to prevent or check spoilage, the causes of spoilage are:

1 excessive growth of micro-organisms, bacterial and fungal;
2 changes due to oxidation, giving poor appearance and flavours;
3 enzymatic or fermentive processes, causing rancidity;( it refers to the spoilage of a food in such a way that it becomes undesirable,and usually unsafe for consumption).
4 drying out (dessication);
5 The metabolism and ripening processes of fruit and vegetables.

Principle of Refrigeration.

When a liquid evaporates a cooling effect is produced. For example, a few drops of volatile liquid i.e. after shave,poured on to the hand gives a cold sensation, as it evaporates rapidly taking heat out of the skin.

Evaporation of leaked water from porous earthen pot surface keeps the water inside the pot surface cool. Similarly if liquid CO2 is made to vaporize at a coil as shown, the heat to vaporize the liquid CO2 will be taken from the surrounding i.e. in this case a bottle of water.
The draw back in the example shown is that the cylinder will soon become empty of liquid CO2 and the cooling effect will stop unless cylinder is recharged with further liquid CO2.

Vapor Compression System

Image credit: http://engineering.myindialist.com
Vapour compression cycle is the most commonly used system of refrigeration. In this system a gas called as refrigerant is used as a medium of heat transfer and is alternately condensed and evaporated to remove heat from the spaces being cooled.

(The temperature at which fluid boils or condenses, is known as saturation temperature and varies with pressure).

The system consists of 4 processes namely:

1. Compression: Compression of the gas is carried out in the compressor, which delivers the gas at high pressure and temperature, raising the saturation temperature, so that it is higher than the sea water temperature or air cooling the condenser.

2. Condensation: The compressed high pressure gas is now condensed to a high pressure liquid in a condenser to below saturation temperature relating to compressor delivery pressure by circulating sea water (or air in case of domestic refrigerators).

3. Expansion: The high pressure liquid is then passed through an expansion valve to reduce its pressure, after passing thru the expansion valve the refrigerant consists of low temperature liquid and a small quantity of vapour both at low pressures.
The pressure drop through the expansion valve causes saturation temperature of the refrigerant to fall so that it will boil at the low temperature of the evaporator.

4. Evaporation: The liquid refrigerant containing small quantity of vapour is now passed thru an evaporator which is located in the space required to be cooled. Here the refrigerant absorbs heat from the surrounding secondary coolant (air or brine) receives latent heat and evaporates, cooling the surrounding space. The evaporated liquid (gas) is passed to the compressor suction for the entire process to repeat itself.

Vapor absorption cycle

Vapor absorption cycle

In the early years of the twentieth century, the vapour cycle of absorption using ammonia water systems was popular and widespread. After the development of vapour compression cycle, the vapour absorption cycle has lost much of its importance because of its low performance (about one fifth of the vapour compression cycle). Today, the steam absorption cycle is mainly used when fuel oil is present, but no electricity.

Absorption Type Refrigeration Unit :
1. Hydrogen vapor which is insoluble in water, leaves the absorber and rises until it meets ammonia liquid falling into entry of evaporator. Due to hydrogen pressure causing lowering of ammonia pressure, this results in vaporization of ammonia.
2. Ammonia and hydrogen vapor are carried down to the absorber where water absorbs and dissolves ammonia and hydrogen vapor re cycles.
3. Ammonia vapor which is highly soluble in water, rises with the water vapor from the generator to the seperator where the water vapor and some ammonia vapor condenses.
4. Ammonia vapor then rises, is liquefied in the condenser, reduced in pressure and vaporized in the evaporator and falls to be absorbed in absorber. Ammonia, dissolved in water, falls down into lower pipe to the generator.
5. Water vapor leaves the generator, is condensed in the separator, falls through the absorber dissolving the ammonia vapor and returning to generator.
The unit requires no compressors or pumps and is silent and vibration less. Condenser, evaporator and vapor liquid separator are air cooled, with fins welded or brazed on to the piping to give extended surface heat transfer.  

AIR-CONDITIONING

The basic principles of air conditioning: Air conditioning is the process of treating air so as to control simultaneously its temperature, humidity, cleanliness and distribution to meet the requirements of the conditioned space. 

Action involved:
Temperature control
Humidity control
Air filtering, cleaning and purification
Air movement and circulation
Winter conditioning relates to increasing temperature and humidity of air whilst summer conditioning relates to decreasing temperature and humidity of air.
What are the objectives of air conditioning on ships ?
1. To extract excess heat
2. To raise air temperature when required
3. To add moisture as required
4. To reduce moisture content as required
5. To maintain sufficient air flow
6. To remove dust


When moisture evaporates from a surface, the latent heat required, is drawn from the surface causing it to be cooled. If a thermometer bulb is covered by a wetted fabric and exposed to the air, the rate of evaporation will depend upon the humidity of the surrounding air. As the heat required must come from the bulb, this results in a lower temperature reading than if the bulb was dry.

Important definitions in air-conditioning:

Hygrometer or Psychrometer: Hygrometer is an instrument to measure the humidity of air. This consists of an ordinary thermometer which gives the dry bulb temperature and a wet bulb thermometer (wetted with gauze cover).The wet bulb reading will be less than the dry bulb reading, the difference is quoted as the wet bulb depression.

The drier the air, the more rapid the moisture evaporation from the gauze giving a cooling effect. Thus greater the difference between the dry and wet bulb readings, drier the air and lesser the relative humidity.

Relative humidity (r.h.): The relative humidity is a measure of the amount of water vapor in the air (at a specific temperature) compared to the maximum amount of water vapor air could hold at that temperature, and is given as a percentage value.

Relative humidity depends on the temperature of the air, as warm air can hold more moisture than cold air. A relative humidity of 100 percent indicates that the air is holding all the water it can at the current temperature and any additional moisture at that point will result in condensation.

A relative humidity of 50 percent means the air is holding half the amount of moisture that it could. As the temperature decreases, the amount of moisture in the air doesn't change, but the relative humidity goes up (since the maximum amount of moisture that cooler air can hold is smaller).

Dewpoint (d,p): is the temperature to which unsaturated air must be cooled to bring it to saturation point and to cause moisture to precipitate. (If an unsaturated mixture of air and water vapour is cooled at constant pressure, the temperature at which condensation of water vapour begins is known as the Dew point.)
Or
The atmospheric temperature (varying according to pressure and humidity) below which water droplets begin to condense and dew can form.
The dew point is the temperature to which the air must be cooled at constant pressure in order for it become saturated, i.e., the relative humidity becomes 100%.
A higher dew point indicates more moisture present in the air.

Physcometry: It is the study of properties of mixture of air and water vapour. This subject is important to air-conditioning because the systems handle air-water vapor mixtures, not dry air.

Some air-conditioning processes involve the removal of water from the air-water vapor mixture (dehumidification) while some involve the addition of water (humidification).

A convenient way to represent the properties of air-water vapor mixtures is the psychrometric chart. On the chart, such properties as dry bulb temperature, wet bulb temperature, dew point, relative humidity, humidity ratio, specific volume, and enthalpy are presented in graphical form.

Comfort Zone chart
 
Comfort Zone: The condition of the air in a space depends on its temperature, humidity and movement. The effect of the air on people in a space varies considerably between one person and another, so it is only possible to stipulate a fairly wide zone.

Under summer conditions relative humidity between 30% and 70%, average about 50% and thermometer readings 19 deg to 25deg, average 22deg gives the best degree of summer comfort.


Ventilation is defined as the circulation of air around a space to clean and refresh it, but not changing the temperature.

Air Velocity: The early air conditioning systems were rather bulky because designs were based on low air velocities in the distribution ducts, with velocities in the order of 10 m/s or less. In later years with very substantial increases in air velocities, reaching a maximum of about 22.5 m/s in the ducts and producing a large reduction in the space occupied by the equipment. Higher velocity systems have increased operating costs but lower installation costs.

What is Low velocity system in ventilation?

A low velocity System is one in which the velocity of air at the beginning of main duct is 5 to 10 m/s and successively lower there after which results in low frictional resistance. Thus in this system we require a fan which is having low power rating, but the only problem with this type of arrangement is that it will require large sized and expensive ducts and installation will be difficult.

What is High velocity system in ventilation?

In high velocity system, velocity of air at the beginning of the main duct is 15 to 30 m/s. Since it includes a high power fan that will produce a high air pressure, it requires small sized ducts and would result in
economy of material,
low manufacturing and installation cost
easy installation on board ship,
considerable space saving in the ship.

This system will have high recurring cost and will also result in high noise levels. Also since the machinery will be running at high speed, the frictional loses in this system will be more.

Typical Air-conditioning System

 Typical Air-conditioning System

The main components of the system, such as the oil separator filter, condenser, expansion valve and evaporator, are explained in the refrigeration system; The components, which are generally unique to the air conditioners, are described below:

Compressor: It can be stroke based or rotatory. In almost all cases, a method for changing the amount of the feed is taken. The piston compressors therefor is also a rotary feed unit for the speed.

Compressor protection: Compressors are under similar protection systems as of refrigiration plant, low pressure cooling zone, high pressure part (manual reset) and this cuts the differential oil pressure. In addition, it has a lock for the compressor installed, can not be started when the air handlink unit fan is not started. When the fan stops, the compressor is turned off.

An alternative is to mount the solenoid valve upstream of the compressor as shown in the diagram above, which only open when the fan is running. The compressor is triggered with a low suction pressure. The purpose is to prevent liquid back to the compressor.

Air handling unit

Air handling unit

In the diagram above a single unit contains an evaporator fed through a gas compressor. A belt driven fan supplies air to the evaporators through an air filter with fine mesh. This filter is removed and washed regularly in a soapy solution containing a disinfectant. The air flows over the evaporator, where it is cooled, and gives water vapor. The water condenses and is transported in a collecting basin and pipelines. The previous draft a collector was installed to remove water droplets entrained in the air, they are not always equipped. A perforated tube is installed after the evaporator allows the low steam quality to be introduced into the air to improve the moisture when it is too dry.

The fresh air is taken from the outside atmosphere and the recirculated air is the return air housing. The air is distributed to the ships during their stay in the port or during navigation normally, Air is recirculated normally on tankers during port stay or during sailing when any cargo or IG related operations are on to prevent cargo vapours from entering the accommodation spaces. For the mass stay at loading port air is taken back for ship carring raw materials such as coal, iron ore etc., To avoid them from entering the air housing.

Thermostat in AC system

A thermostat is the component of an Air-con system which regulates the temperature of the space to be cooled so the temperature is maintained near a desired set point temperature. The thermostat does this by indirectly switching the compressor on or off, to maintain the correct temperature.

As long as the desired temperature in the accommodation space is not reached the Air con compressor keeps working and thereby cooling the accommodation, when the desired temperature is reached the thermostat actuates and closes the liquid line magnet valve(solenoid valve) located on liquid line after the condenser, the compressor then eventually stops on low suction pressure cut off. However the air handling unit blower keeps running all the time.

Now as the accommodation temperature starts going up above the desired set point the thermostat energizes the liquid line magnet valve, the suction pressure now goes up as the gas starts flowing to the compressor, the compressor then immediately starts on L.P cut in thereby the cooling now again commences, this cycle is repeated to maintain the desired temperature in the accommodation spaces.

Thermostats are normally located in the air handling unit; they sense the temperature of Return air. Alternately they are also located in one of the cabins on the top deck.

Recently, digital thermostats have no moving parts to measure the temperature, and instead rely on thermistors or other semiconductor devices, such as a resistance thermometer (resistance temperature sensor). Each has an LCD screen that displays the measured temperature and the set temperature.

What is Capacity Control?
Capacity control of an air-conditioning plant can be defined as a system which controls the output of the plant as per the load in demand. Refrigerating capacity control with reciprocating compressors running at constant speed consists of controlling the quantity of gas delivered to match the fluctuating load

Holding the valves open: This is the most common method used in unloading in multi cylinder V & W type compressors. It is accomplished by lifting of suction valves, usually of 2 cylinders together by means of push pins. When the suction valve is lifted the gas drawn during suction stroke is pushed back into the suction line during the upward stroke of the piston. No work is done except frictional work during such idling. The push pins are operated by oil pressure. More and more cylinders are unloaded as the suction pressure or evaporator temperature continues to drop.
Normally in warm weather area the AC plant is always running at full load, ideally the air conditioning plant will start unloading when the ship goes into colder weather. The thermostat control will come into action only when further drop in temperature takes place, and this will stop the air-con compressor.

#Cover Image credit: Chitre Sir (Marine Faculty) / If you have any problem regarding post, please contact us!

# Various books, study material and other online sources has been refereed prior to writing this article but no part is copied or produced  from any of the source but explained same thing in better detailed way.

Author: Amit                                                                Article Requested by: Pranesh Devadiga


STCW & SHIP FIRE PREVENTION

STCW & SHIP FIRE PREVENTION

FIRE TRIANGLE: IF ANY ONE SIDE OF “FIRE TRIANGLE” IS REMOVED, FIRE WILL BE EXTINGUISHED.
METHODS OF FIRE FIGHTING: THERE ARE FOUR METHODS OF FIGHTING FIRE
  • SMOTHERING – REMOVING THE AIR.
  • STARVING - REMOVING THE BURNING MATERIAL FROM THE SURROUNDING.
  • COOLING – REMOVING THE HEAT.
  • INHIBITING – RETARDATION OF THE COMBUSTION REACTION.
FIRE TRIANGLE

Types of fire

In the European Standard "Classification of fires" (EN 2:1992, incorporatiing amendment A1:2004), the fires are classified as:
Class A fire: Ordinary combustibles such as wood, paper, carton, textile, and PVC;
Class B fire: Flammable liquids and solids which can take a liquid form, such as benzene, gasoline, oil;
Class C fire: Flammable gases, such as butane, propane, and natural gas;
Class D fire: Combustible metals, such as iron, aluminum, sodium, and magnesium;
Class F fire: Cooking media, such as oils and fats, in cooking appliances;
A fire involving energized electrical equipment is not classified by its electrical property.

SHIP FIRE PREVENTION

SMOTHERING

IF THE OXYGEN CONTENT OF THE ATMOSPHERE IN THE IMMEDIATE NEIGHBORHOOD OF BURNING MATERIAL CAN BE SUFFICIENTLY REDUCED COMBUSTION WILL CEASE. THIS PRINCIPLE IS INEFFECTIVE IN THE CASE OF CELLULOID AND SIMILAR SUBSTANCES, WHERE BURNING OF THE MATERIAL CONTAINS WITHIN ITSELF, IN A CHEMICALLY COMBINED FORM.

PRACTICAL ASPECT: ON A SMALL SCALE IT IS EMPLOYED IN A SNUFFING  CANDLE. PERSONS CLOTHING CAN BE SMOTHERED WITH A RUG / BLANKET
ON A LARGE SCALE, IN CAPPING A BURNING WELL. BATTERING DOWN OF A SHIP’S HOLD WHEN A FIRE BREAKS OUT BELOW DECKS WILL OFTEN HOLD THE FLAMES IN CHECK UNTIL PORT IS REACHED.

PRACTICAL APPLICATION OF SMOTHERING METHOD
  • USE OF FOAM: THIS FORMS A VISCOUS COATING OVER THE BURNING MATERIAL AND LIMITS THE SUPPLY OF AIR.
  • USE OF DRY POWDER: SODIUM BICARBONATE FROM A PRESSURIZED EXTINGUISHER. CARBONATE WHEN FINELY DIVIDED ABSORB HEAT AND THUS HAS COOLING AND FLAME INHIBITING EFFECT.
  • USE OF INERT GAS: THE VIGOROUS DISCHARGE OF INERT GAS, SUCH AS CARBON DIOXIDE & NITROGEN IN THE IMMEDIATE VICINITY OF THE FIRE REDUCES THE OXYGEN CONTENT OF ATMOSPHERE BY PROVIDING A TEMPORARY BLANKET EFFECT.

STARVATION

THE EXTINCTION OF FIRE BY STARVATION IS APPLIED IN THREE WAYS. BY REMOVING COMBUSTIBLE MATERIAL FROM THE NEIGHBORHOOD OF THE FIRE. 
Ex: DRAINING OF FUEL FROM BURNING OIL TANKS, DISCHARGING OF CARGO AT A SHIP FIRE.
BY REMOVING THE FIRE FROM THE NEIGHBOURHOOD OF COMBUSTIBLE MATERIAL.
Ex: PULLING APART A BURNING HAYSTACK.
BY SUB-DEVIDING THE BURNING MATERIAL. 
Ex: SMALLER FIRES PRODUCED MAY BE EXTINGUISHED MORE EASILY, SUCH AS EMULSIFICATION OF THE SURFACE OF BURNING OIL.

COOLING

THE PROCESS OF REMOVING THE HAET FROM FIRE IS CALLED COOLING. THIS IS NORMALLY DONE BY WATER, AS WATER HAS MORE COOLING EFFECT AND VERY HIGH LATENT HEAT. APPLICATION OF JET OR SPRAY OF WATER TO A FIRE, EMULSIFICATION OF THE SURFACE OF OIL BY MEANS OF THE EMULSIFYING TYPE OF SPRINKLER HEAD.

INHIBITING

IN THIS HEAT PRODUCING CHEMICAL REACTION OF SUBSTANCES IS CHECKED OR STOPPED. THIS APPLIES TO ONLY FLAMING MODE AND NOT TO THE GLOWING MODE. IN THIS FLAME INHIBITING EXTINGUISHING MEDIUM INTERFERES WITH THE ACTIVE SPECIES IN FLAME CHAIN REACTION WHICH WOULD OTHERWISE FUNCTION AS “CHAIN CARRIERS”. THIS METHOD EXTINGUISHES THE FLAME VERY RAPIDLY.
    Ex: DCP OR HALON GAS – THESE ACT BY CHEMICAL INTERFERENCE WITH THE CHAIN REACTION OF FLAME PROPAGATION.

PROPERTIES OF FLAMMABLE MATERIAL

FLAMMABILITY: THIS IS THE ABILITY OF SUBSTANCE TO BURN. IN THIS VAPOR GIVEN OFF BY FLAMMABLE MATERIAL CAN BURN WHEN MIXED WITH AIR IN THE RIGHT PROPORTION IN THE PRESENCE OF AN  IGNITION SOURCE.

IGNITION POINT: IT IS THE LOWEST TEMP., TO WHICH A FLAMMABLE SUBSTANCE MUST BE HEATED TO IGNITE.

FLASH POINT: IT IS THE LOWEST TEMP., AT WHICH THE VAPOUR OF THE SUBSTANCE ARE AVAILABLE IN SUFFICIENT QUANTITY TO PRODUCE A MOMENTARY FLASH WHEN A FLAME IS APPLIED.

FIRE POINT: IT IS THE TEMP., AT WHICH THE HEAT FROM THE COMBUSTION OF BURNING VAPOR IS CAPABLE OF PRODUCING SUFFICIENT VAPOUR TO ENABLE COMBUSTION TO CONTINUE.

SPONTANEOUS / AUTO / SELF IGNITION TEMP: IT IS THE LOWEST TEMP., AT WHICH THE SUBSTANCE WILL IGNITE SPONTANEOUSLY i.e., THE SUBSTANCE WILL BURN WITHOUT THE INTRODUCTION OF A FLAME OR OTHER IGNITION SOURCE.

UPPER FLAMMABLE LIMIT: IT IS THE CONCENTRATION OF FLAMMABLE VAPOUR IN AIR ABOVE WHICH THE MIXTURE BECOMES TOO RICH TO IGNITE AND PROPEGATE COMBUSTION.

LOWER FLAMMABLE LIMIT: IT IS THE CONCENTRATION OF FLAMMABLE VAPOUR IN AIR BELOW WHICH THERE IS INSUFFICIENT FLAMMABLE VAPOUR TO SUPPORT AND PROPAGATE COMBUSTION.

STATIC ELECTRICITY: IT IS THE ELECTRICITY PRODUCED IN DISSIMILAR MATERIALS THROUGH PHYSICAL CONTACT AND SEPARATION i.e., A SAMPLING APPARATUS LOWERED IN TO A TANK CONTAINING CHARGED PETROLEUM LIQUID.

FLAMMABLE RANGE: IT IS THE RANGE OF CONCENTRATION OF A FLAMABLE VAPOUR IN AIR WITH WHICH THE VAPOUR AND AIR MIUXTURE IS FLAMABLE.

FLAMMABILITY: IT IS THE ABILITY OF SUBSTANCE TO BURN VAPOUR GIVEN OFF BY A FLAMMABLE MATERIAL, WHEN MIXED WITH AIR IN RIGHT PROPORTION IN THE PRESENCE OF THE IGNITION SOURCE. NORMAL AIR CONTAIN -  21%  OF O2  AND 78% OF N2 AND SMALL TRACES OF CO2 , WATER VAPOUR etc. IN CARGO TANKS AS THE PERCENTAGE OF HYDROCARBON INCREASES, OXYGEN CONTENT DECREASES.

LOWER FLAMABLE LIMIT (LFL): FOR A MIXTURE OF AIR AND THE FUEL TO BE COMBUSTIBLE, MINIMUM QUANTITY OF THE FUEL VAPOUR SHOULD BE PRESENT IN THE MIXTURE. THIS IS EXPRESSED AS PERCENTAGE OF FUEL VAPOUR IN THE MIXTURE OF AIR AND VAPOUR. THIS IS CALLED LOWER FLAMABLE LIMIT. THE MIXTURE WILL NOT BURN UNLESS FUEL VAPOUR CONTENT IN THE COMBUSTIBLE MIXTURE IS ABOVE LFL.

EVERY TYPE OF FUEL HAS DIFFERENT LFL.
POINT “F” – MINIMUM OF O2 REQUIRED FOR COMBUSTION  ( 11% BY VOLUME).
    LFL – LOWER FLAMABLE LIMIT
          – 1% OF C2H2 AT POINT “A”

Flamablity Diagram

UPPER FLAMABLE LIMIT (UFL):
WHEN THE PERCENTAGE OF FUEL VAPOUR IS INCREASED IN THE MIXTURE, THE PERCENTAGE OF AIR AND HENCE THE PERCENTAGE OF OXYGEN REDUCES.
SINCE THE OXYGENN CONTENT BELOW 11% IN THE MIXTURE DOES NOT SUPORT COMBUSTION, A STAGE MAY BE REACHED WHEN THE PERCENTAGHE OF VAPOUR IN THE MIXTURE IS SO HIGH THAT RESULTING PERCENTAGE OF OXYGEN IS TOO LOW TO SUPORT THE COMBUSTION AND MIXTURE WOULD NOT BURN EVEN WHEN IGNITED. THIS IS CALLED UPPER FLAMABLE LIMIT.
MIXTURE WILL NOT BURN IF THE FUEL VAPOUR CONTENT MORE THAN THE UFL.
UFL – UPPER FLAMABLE LIMIT
              - 11% OF C2H2 AT POINT “B”

EVERY FUEL HAS A LFL and UFL AND THE PERCENTAGE OF FUEL VAPOUR RANGE BETWEEN BETWWEN THESE TWO LIMITS IS CALLED “FLAMABLE RANGE”
POINT “A” – AT THE END OF BURNING IF THE PRODUCT OF COMBUSTION ARE ANALYSED, IT IS FOUND THAT ALL OF C2H2 VAPOURS ARE CONSUMED, WHILE SOME “O2” IS UNUSED AND STILL AVAILABLE.
POINT “B” – AT THE END OF BURNING, ON ANALYSIS, IT IS FOUND THAT ALL OF “O2” IS CONSUMED AND SOME UNBURNT C2H2 IS STILL AVAILABLE.

SOURCE OF IGNITION  (HEAT ENERGY)

  1. CHEMICAL HEAT ENERGY
  2. ELECTRICAL HEAT ENERGY
  3. MECHANICAL HEAT ENERGY
  4. NUCLEAR HEAT ENERGY
CHEMICAL:
  • HEAT OF COMBUSTION
  • HEAT OF PARTIAL OXIDATION
  • SPONTANEOUS HEATING
  • HEAT OF DECOMPOSITION (ONION, POTATO etc., IN CARGO HOLD)
  • HEAT OF SOLUTION (MIXTURE OF TWO CHEMICALS)
  • ELECTRICAL:
  • RESISTANCE HEATING
  • DI-ELECTRIC HEATING
  • INDUCTION HEATING
  • MECHANICAL:
  • FRICTIONAL HEATING
  • FRICTIONAL SPARKS
  • HEAT OF COMPRESSION

CLASSIFICATION OF FIRE

FIRES ARE CLASSIFIED ACCORDING TO THE TYPES OF MATERIAL WHICH ARE ACTING AS FUEL. FIRES BURNING WOOD, GLASSFIBRE, UPHOLSTERY AND FURNISHINGS. FIRES BURNING LIQUID SUCH AS LUBRICATING OIL AND FUELS. FIRES BURNING GAS FUELS SUCH AS LIQUIFIED PETROLEUM GAS. FIRES BURNING COMBUSTIBLE METALS SUCH AS MAGNESIUM AND ALUMINIUM. FIRES BURNING ANY OF THE ABOVE MATERIALS TOGETHER WITH HIGH VOLTAGE ELECTRICITY.

THESE CLASSIFICATIONS ARE ALSO USED FOR EXTINGUISHERS AND IT IS ESSENTIAL TO USE THE CORRECT CLASSIFICATION OF EXTINGUISHER FOR A FIRE, TO AVOID SPREADING THE FIRE OR CREATING ADDITIONAL HAZARDS. MANY FIRE EXTINGUISHER WILL HAVE MULTIPLE CLASSIFICATIONS SUCH AS A, B and D

FIRE EXTINGUISHING AGENTS

FIRE EXTINGUISHING AGENTS

CARBON DIOXIDE: AT NORMAL TEMP., CO2 IS 1.5 TIMES HEAVIER THAN AIR. IT IS EASILY LIQUEFIED AND BOTTLED. IT IS STORED UNDER PRESSURE OF 50bar IN STEEL CYLINDERS. WHEN CO2 IS APPLIED TO FIRE, THE LIQUID CO2 BOILS OFF RAPIDLY AS A GAS, EXTRACTING HEAT FROM THE SURROUNDING ATMOSPHERE. IT EXTINGUISHES FIRE BY SMOTHERING i.e., BY DISPLACING OXYGEN. ABOUT 20-30 % OF THE ATMOSPHERE SHOULD CONTAIN CO2 TO EXTINGUISH THE FIRE. CO2 IS QUICK AND CLEAN, NON-TOXIC, DOES NOT HARM MOST FAFRIC AND DOES NOT CONDUCT ELECTRICITY. SO IT CAN BE USED ON ELECTRICAL IT DOES NOT DAMAGE EXPENSIVE CARGO OR MACHINERY. IT LEAVES NO UNDESIRABLE RESIDUE TO BE CLEARED OFF AFTER USE. SO IT CAN BE USED TO EXTINGUISH FIRE IN CARGO AND MACHINERY SPACES BY PROVIDING FIXED CO2 INSTALLATIONS.

ADVANTAGES OF CARBON DIOXIDE:
  1. NON-CORROSIVE.
  2. DOES NOT CONDUCT ELECTRICITY.
  3. LEAVES NO RESIDUE.
  4. EASILY AVAILABLE.
  5. NOT SUBJECTED TO DETERIORATION IN QUALITY WITH AGE.
DISADVANTAGES OF CARBON DIOXIDE:
  1. TOXIC AND HAZARDOUS TO HUMAN BEING.
  2. LITTLE COOLING EFFECT & DANGER OF RE-IGNITION IF AIR IS READMITTED IN ROOM.
  3. SOLID CO2 PARTICLES GENERATE SPARK DUE TO STATIC ELECTRICITY, SO UNSUITABLE IN OIL TANKERS
WATER: IT IS MOST EFFICIENT , CHEAPEST AND READILY AVAILABLE MEDIUM. IT HAS A COOLING EFFECT AND NO-TOXIC. IT ABSORBS HEAT AND EXPANDS TO 1700 TIMES OF IT’S VOLUME TO PRODUCE STEAM WHICH HAS SMOTHERING EFFECT.
IT IS SAFE TO USE ON MOST OF THE FIRES, IT CAN BE EASILY DIRECTED OVER A CONSIDERABLE DISTANCES.

DISADVANTAGES:
  1. IT CONDUCTS ELECTRICITY.
  2. IT CAN CAUSE DAMAGE TO CARGO & MACHINERY.
  3. LOSS IN STABILITY OF SHIP WHEN USED IN LARGE QUANTITY.
FOAM:
IT IS MOST SUITABLE FOR EXTINGUISHING FIRES INVOLVING FLAMMABLE LIQUIDS. IT EXTINGUISHES BY FORMING A LAYER OF SMALL BUBBLES ON THE SURFACE OF THE LIQUID PREVENTING FUEL FROM VAPOURISING AND RESTRICTING THE OXYGEN SUPPLY TO IT.
IT IS INSOLUBLE IN MOST OF THE LIQUIDS AND LIGHT IN WEIGHT, SO IT FORMS A BLANKET TO COVER THE SURFACE OF BURNING LIQUID AND THUS EXTINGUISHES THE FIRE.

FOAM CAN BE GERATED BY MECHANICAL OR  CHEMICAL MEANS.
MECHANICAL FOAM IS GENERATED BY AGITATION OF A DILUTED FOAM COMPOUND SOLUTION IN PRESENCE OF AIR. THESE COMPOUND INCLUDE SOAPS, GLUE AND WETTING AGENT MIXTURES. CHEMICAL FOAM IS GENERATED BY MIXING AN ALKALI (SODIUM BI-CARBONATE) WITH A SOLUTION OF ALUMINIUM SULPHATE, IN PRESENCE OF A STABILIZER (i.e., SOAP) THIS PRODUCES SKIMMED BUBBLES CONTAINING CO2 “HIGH EXPANSION FOAM” HAS A VERY HIGH EXPANSION RATION OF AROUND 1000 TO 1 INSTEAD OF 8 TO 1 FOR STANDARD FOAM. THIS TYPE FOAM IS USED FOR DEALING WITH CARBONACEOUS FIRES IN COMPARTMENTS WHICH ARE INACCESSIBLE AND WHICH LEND THEMSELVES TO COMPLETE FLOODING  OF THE COMPARTMENT.

DRY CHEMICAL POWDER:
WATER CANNOT BE USED ON MOST FIRES AS IT CAN BE EXPLOSIVELY DISASTROUS. IN VIEW OF THIS OTHER MEDIUMS ARE USED. CHIEF AMONG THEM IS DRY CHEMICAL POWDER. IN THIS SODIUM BICARBONATE IS USED AS BASIS ALONG WITH ADDITION OF METALLIC STEARATE AS WATER PROOFING AGENT. DRY CHEMICAL POWDER IS EXPELLED FROM CONTAINER BY GAS PRESSURE.

IT IS ESPECIALLY EFFECTIVE ON BURNING LIQUIDS SUCH AS LIQUIFIED GAS, OIL ESCAPING FROM LEAKING LINES AND JOINTS. ON ACCONT OF IT’S UNIQUE ABILITY TO QUICKLY STOP COMBUSTION OF GASES, CHEMICAL PRODUCTS etc., IT HAS BECOME MOST POPULAR MEDIUM IN GAS CACCIERS AND TANKERS. DRY CHEMICAL POWDER IS ELECTRICAL NON-CONDUCTOR , THUS IT CAN BE UTILISED ON FIRES INVOLVING LIVE ELECTRICAL EQUIPMENTS. IT INHIBITS THE COMBUSTION REACTION.

Solas convention

The International Convention for the Safety of Life at Sea (SOLAS) is an international maritime safety treaty. It ensures that ships flagged by signatory States comply with minimum safety standards in construction, equipment and operation.

1974 version
The intention had been to keep the Convention up to date by periodic amendments, but the procedure to incorporate the amendments proved to be very slow,As a result, a complete new convention was adopted in 1974 which includes all the agreements and acceptable procedures. Even though the Convention was updated and amended numerous times, the Convention in force today is sometimes referred to as SOLAS, 1974.

The latest Convention in 1974 included the "tacit acceptance" procedure whereby amendments enter into force by default unless nations file objections that meet a certain number or tonnage.

Types of Bulkheads.

'A' Class Divisions
Class differences "A" are the bulkheads and decks of steel or any other equivalent material which is capable of preventing the passage of smoke and flames to the end of the test standard of the hour of fire. They are well reinforced. They are insulated with unauthorized combustible materials so that the average temperature of the un-exposed side does not rise above the initial temperature or temperature at any point above 140 ° C, including any junction, rise above 180 ° C above the original temperature, Within the time, specified below:

"A-60" 60 minutes

"A-30" 30 minutes

"A-15" 15 minutes

"A-0" 0 minutes.

A prototype or platform partition should be tested according to the FireCode test procedure to ensure that it meets the above requirements for integrity and temperature rise.

Class A fire protection doors

The construction of the doors in the class A walls and the fastening means in the closed position provides a fire resistance, such as the passage of smoke and flames, as far as possible, similar to the bulkheads in which they are located.

Class A fire-resistant doors, made of steel or an equivalent material.

In These doors should be capable of being opened and closed from each side of the bulkheadby one person only.
Fire doors in main vertical zone bulkheads, galley boundaries etc., other than power operated water tight doors should be (1) self closing and and be capable of safe operation with an angle of inclination of upto 3.5 degrees opposing closure, and in no more than 40 sec. and no less than 10 sec. with the ship in upright position. (3) the doors except for those for emergemcy escape trunks Shall be capable of of remote release from the central control stations and should also be capable of release individually from a position at both sides of the door.  Release switches shall have an on-off function to prevent automatic resetting of the system.  (4) hold back hooks not subject central control station release are prohibited, (5) a door closed remotely shall be capable of being reopened locally from both sides of the door and after such opening, the door shall automatically close again.(6) there should be fire door position indicator on the indicator .

Indicator panel in the central control room and the release mechanism shall be so designed that the door will automatically close in the event of power supply failure. (7)  local power supply accumulators for power operated doors shall be provided in the immediate vicinity of the doors to enable the doors to be operated at least 10 times (open and close)  after  disruption of the control system or the central power supply using local controls. (8) the components of the local control system shall be accessible for maintenance and adjusting.

(9) In the event of a fire, the control system shall operate the door at the temp. of at least 200 deg. For at least 60 min. served by the power supply and the power supply for all other doors not subject to fire shall not be impaired, and (10) at temperatures  exceeding 200 deg. C the control system shall automatically be isolated from the power supply and shall be capable of keeping the door closed upto at least 945 deg.C.

'B' Class Divisions
Class differences "B" are the bulkheads, decks, blankets and coatings

Approved non-combustible materials to prevent sufficient flame to pass through the end of the first half hour of the standard fire test. They have an insulation value so that the average temperature of the un-exposed side does not exceed 140 ° C above the initial temperature or the temperature at any point, including any junction, rises more than 225oC to the initial temperature, the following phases:

Class "B-15" 15 minutes

Class "B-0" 0 minutes.

A prototype or platform partition should be tested according to the FireCode test procedure to ensure that it meets the above requirements for integrity and temperature rise.
 
Class B fire protection doors

The construction of all doors in the partition type "B" and the means in the closed position represents the equivalent of fire as far as possible bulkheads in which the doors of the exception that can lie vent openings in the lower part of the doors, with a total area of ​​the lower opening Or equal to 0.05 m2. (1) These doors must be closed. Retaining hooks are not permitted. The doors of class B fire must be built with non-flammable materials approved. Class B fire protection doors built with approved non-combustible materials in accordance with the test method Code for fire.

Class differences, C '

Class differences "C" are the non-flammable materials, the bulkheads, decks, ceilings and linings, which limit requirements for the passage of smoke and flames or temperature rise. Door Class "C" is the type of doors installed in the class partitions "C". The approved noncombustible materials must be constructed.

Fire dampers

Valves are penetrating into the ventilation ducts installed bulkheads and bridging the class "A" to maintain the division of fire resistance capability and prevent the spread of smoke and flames in adjacent compartments through the ventilation system.

fire integrity

Resistance to fire is to keep the grounding element's resistance with a bulkhead or deck intact for a period of time, 60 minutes for class "A" and 30 minutes for class "B".

Fire Detection Systems

The PURPOSE of this regulation is to detect a fire in the space of origin and to provide for alarm for safe escape and fire fighting activity.  For this purpose :
(1) Fixed Fire Detection  and fire alarm system installations shall be suitable for the nature of the space,fire growth potential  and potential generation of smoke and gases, (2)  manually operated call points shall be placed effectively to ensure a readily accessible means of notification and (3) fire petrols shall provide an effective means of detecting and locating fires and alerting the navigation bridge and fire teams.  Fire Detection Systems. – General Requirements.

A fixed fire detection and alarms system shall be provided as per this regulation.
 A fixed fire detection and alarm system and a sample extraction smoke detection system required as per regulations mentioned in Chapter II-2, Part C, of SOLAS shall be of an approved type and comply with Fire  Safety Systems Code.
The function of such systems shall be tested under varying conditions of ventilation after installation.
Such installed systems shall be periodically tested for proper functioning under simulated fire conditions to the approval of Administration.

Detection in Machinery Spaces:
A fixed fire detection and fire alarm system shall be installed in (i) periodically unattended machinery spaces and (ii)m/c spaces containing all automatic and remote control systems and equipment approved in lieu of continuous manning of the space and also  in continuously manned spaces having a central control room.
This system shall be so designed and installed that all the fire detectors  of  suitable type will be capable of detecting the smoke or fire rapidly in any part of the spaces under working varying condition of temperature and ventilation.

Detection in Accommodation and Service Spaces and Control Stations:
(1)  Smoke detectors shall be fitted in all stairways, corridors, and escape routes and if found necessary, special purpose smoke detectors shall be fitted within ventilation ducting.

Fire Extinction Systems. – General Requirements
This system is brodadly divided in three parts:
Regulation 8 of Part C of Chapter II-2 of SOLAS.  Control of Smoke spread :  For this purpose, means of controlling smoke in atriums, control  m/c spaces and concealed spaces shall be provided.
For example, in most cargo ships of any type of all the supply air fans (usually 4) for machinery spaces, at least one fan is reversible and can be used as an exhaust fan in the event of fire and generation of smoke in the m/c spaces.
In accommodation, gallies, Navigation Bridge, Steering Flat  a provision for exhaust fans is made to expel smoke from the concerned spaces.

(2) Regulation 9 of Part C of Chapter II-2 of SOLAS.
Containment of Fire:  For this purpose (i) the ship shall be subdivided by thermal and structural boundaries,
 (ii) thermal insulation of boundaries shall have due regard to the fire risk of the space and adjacent spaces,
(iii)  The fire integrity of the divisions shall be maintained at openings and penetrations by using approved materials and methods by adhering to the relevant regulations of the SOLAS.

(3) Regulation 10 of Part C of Chapter II-2 of SOLAS.
Fire fighting:  For this purpose, following functional requirements will be met : (A) fixed fire extinguishing systems shall be installed, having due regard to the fire growth potential of the protected spaces, and (B) adequate number of approved type of fire extinguishing appliances shall be readily available.
 (C) Water supply systems  with approved type and sufficient number of fire pumps, fire mains, hydrants, hoses and nozzles complying with the regulations of the SOLAS requirements shall be provided.

(i)  Fire mains and hydrants materials readily rendered ineffective by heat shall not be used.
(ii) Their arrangement shall be such as to avoid the possibility of freezing, with adequate provisions for the drainage of the mains.
The number and position of hydrants should be such that at least two jets of water from two different hydrants may reach any part of the ship.
There will be an  isolating valve and a relief valve on the fire main line as approved by the regulations.
Pressure at the hydrants: For cargo ships above 6000 grt   it should be 0.27N/mm2.

(vi) Fire pumps : For cargo ships of 1000 grt  and above, there will be at least two independently driven fire pumps, which will  have the provision for being started and stopped by local and remote  switches (normally situated on the Bridge).
Emergency fire pump :  The space containing the emergency fire pump shall not be contiguous to the boundaries of the m/c spaces  or those spaces containing main fire pumps.  There will be no direct access between the m/c space and the emergency fire pump spaces.
The emergency fire pump shall have two sources of electrical power supply, one from the power mains and the other from the emergency generator bus bars.
Ventilation arrangements to the emergency fire pump spaces shall be such as to preclude the possibility of smoke from m/c space fire entering or being drawn into the space.
(viii) Fire hoses shall be of non perishable material  approved by the Administration and should have a length of at least 10 mtrs, but not more than 15 mtrs in m/c spaces and not more than 25 mtrs for open  decks on ships with breadth in excess of 30 mtrs.
(ix) Standard nozzle sizes shall be 12mm, 16mm and 19 mm.  For accom. Spaces a nozzle size greater than 12 mm and for cargo spaces a nozzle size greater than 19 mm need not be used.  The size should be adequate to obtain the max. discharge possible from two jets at the approved pressure.  Nozzles shall be of approved dual purpose type( i.e. spray/jet) incorporating a shut off.
(x) Portable fire extinguishers:  Their type and design shall comply with the requirements of the Fire Safety systems Code.
Ships of 1000 grt annd above will have at least 5 portable fire extinguishers in accom. Spaces, service spaces and control stations.  CO2  fire extinguishers shall not be placed in accom. Spaces.  In control stations and other spaces containing electrical or  Or electronic equipment, only those fire extinguishers whose extinguishing media are not electrically conductive or harmful  shall be used.
Spare charges shall provided for 100% of the first ten extinguishers and 50% for the remaining fire extinguishers capable of being recharged on board. Instructions for recharging shall be carried on board.
(xi) Fixed fire extinguishing systems: These systems for m/c spaces may be any of the following types: Fixed gas fire extinguishing system, a fixed high expasion foam fire extinguishing system or a fixed pressure water spraying fire extinguishing systems, all complying with the provisions of the Fire Safety Systems Code.

Here fire extinguishing systems using Halon 1211, 1301, and  2402 and perfluorocarbons shall be  prohiibited.
(xii) There shall be at least one portable foam applicator unit complying with the provisions of the Fire Safety Systems Code.  In addition, in each space, approved foam type fire extinguishers each of at least 45 ltr capacity shall be provided.  Additionally, there shall be provided a sufficient number of portable foam extinguishers so located that no point in the space more than 10 m walking distance from an extinguisher and that there are at least two such extinguishers in each space.
(xiii) Paint Lockers shall be protected by  (i) Co2 system designed to give a minimum volume of free gas equal to 40% of the gross volume of the paint locker, (ii) a dry powder system giving at least 0.5 kg powder/m3 of the space, (iii)  a water spraying or sprinkler system connected to ship’s fire mains designed for 5 ltr/m2 /min.  All above systems shall be operable from outside the protected space.
(ivx)  Fire Extinguishing systems for cargo spaces:  Fixed Co2 or inert gas system complying with the provisions of the Fire Safety System Code.  For cargo tank protection on Tankers a fixed deck foam fire extinguishing systems complying with provisions of the Fire Safety System Code shall be used.
(xv) Approved Fire Fighter’s Outfits (atleast two in  nos.) shall be carried by all ships.  Additionally, on tankers two extra sets will be carried.

 # The article was written by two author and then merged before publishing. Various books are used as reference before writing this article but no part is being reproduced but stated in a different easy way.

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Author Arpit Singh & Amit