Showing posts with label boiler. Show all posts
Showing posts with label boiler. Show all posts

Monday, April 16, 2012

Marine engineering starting of boiler


Marine engineering starting of boiler 

  • 1.  
  • 2. IT IS THE ALLAH WHO SUBJECTED THE SEA TO YOU.THAT SHIP MAY SAIL THROUGH IT BY HIS COMMAND ,THAT YE MAY SEEK OF HIS BOUNTY,AND THAT YE MAY BE GRATEFUL (Al-Quran)
  • 3. Marine Engineering Starting of boiler
  • 4. Starting of boiler Start the forced draft(FD) fan Start the air purge at least 3 minutes. Drain the atomizing steam Open the atomizing steam or admit air for atomizing of fuel. Start diesel oil pump Push the nozzle inside the burner Push the ignitor inside the burner Now ignite the fuel with spark ignitor. Incase of misfire reapeat no.2
  • 5. Note Purge the boiler at least 3 minute before routine starting up or incase of misfire. Drain the atomizing steam If any unusual case is happened inform the duty engineer.
  • 6. Author Introduction ZEESHAN AHMED , Marine Engineer . After doing FSc(pre-engineering) from PAF(fazaia) intermediate college Lahore cantt. I joined Pakistan Marine Academy and choose Marine engineering branch. Two years of training at academy (practical + theoretical) we learned a lot of thing like CNC (computerize numeric code), trained on various models (like control valve, solenoid valve, flow meter, refrigeration system, CPP propeller, Main engine model (TWO stroke), Boiler model (water tube) ……………………………….. in GEK (general engineering knowledge) lab, Mechanical and physics lab, Engineering workshop. ETC . After two years, we joined PNSC workshop for the training of ONE year Industrial training. That was also the golden time where we learnt a lot of things at different shops as well as onboard (repairing and watch keeping). I learn many thing on tanker E.g. MT Johar (learn how to dismantle turbine rotor from casing and what are the precautionary measurement while working on turbine, learn how to change the diaphragm(stationary blade) Plate type heat exchanger gasket change, shell and tube Cooler Anode replacement and (Cont.)
  • 7. Introduction (cont.) cleaning of SALT WATER tubes etc.) , MT Swat (major thing which I learn in Swat is how to dismantle head of main unit and copper gasket replacement with a minor facing defect which is found during overhauling which is filled and faced by Belzona) , MT Lahore(About the DEAD MAN ALARM, Alpha lubricator for Cylinder Main Engine Unit, Pump operation and watch keeping), MT Quetta(Auto load sharing of Generator Set, MT Karachi (Dry washing of the main engine turbocharger with granules, water washing of IG Fan of Inert Gas system, sludge removal of from purifier(centrifuge) etc., . One thing I want to added is that the trend in ship building is more toward based on electronic and electrical application. So a marine engineer must strong in automation, instrumentation and control system. PLC (programmable and logic control) and SCADA (supervisory central access and data acquisition) are the upcoming technology that are using on modern ship. The latest engine of MAN B&W is based on Camless technology. Chain is removed ; fuel pump and exhaust valve actuation is control by hydraulic servo(lub) oil which is driven by Axial piston pump mounted on the Fly wheel. Regards, Z.A.
  • 8. Author contact information zeetec4@yahoo/gmail/hotmail.com Social networking sites. Facebook: mariner46 Website: zeetec4.googlepages.com Any question and suggestion are welcome

Wednesday, November 30, 2011

Boiler Control System

Boiler Control System
The boiler control panel provides operation, control and interlock devices
required for the safe running of the boiler. This control panel directs the
performance of all functions required for automatic operation of the boiler and
provides a central control point for manual operation. The control system also
features a network of alarms which give warning if an abnormality occurs
during boiler operation.
In the event of a serious abnormality occurring, which would make it unsafe
for the boiler to continue in operation, the boiler automatic control system
shuts down the boiler in an emergency mode, by immediately shutting down
the fuel oil supply to the boiler.
Control Panels
ECR Console Remote Indication Panel
This indication panel is installed in the engine control room and it mimics the
monitoring systems and main controls found at the boiler and boiler side
control panel.
The ECR console has the following items:
Drum level indicator
Steam drum pressure indicator
Smoke indicator
Emergency stop switch
Burner run lamp
Lamp test switch
Boiler Side Boiler Control Panel
This control panel is installed at the boiler side. It contains the system power
supply unit, the sequence control for operation of the burner, the automatic
boiler controller and various necessary relay units.
The following alarms are mounted on the control panel :
Electrical AC power source failure
Burner start sequencer inactive
Manual trip
FD fan trip
Pilot pump abnormal
Drum level low-low
Atomising pressure low
Ignition fail
Flame fail
Flame eye abnormal
Burner piston valve abnormal
FO pressure low-low
Control air pressure low
Burner Control System
The boiler control panel (BCP) operates in a number of functions associated
with the boiler including the boiler management system (BMS), automatic
combustion control (ACC), and feedwater control (FWC). There are two
boilers and they are controlled on a master/slave basis with one of the boilers
being designated the master by the control system and the other the slave.
Under normal circumstances the master boiler would operate to supply the
ship's steam requirements but if it cannot meet demand the slave boiler is
started and comes under the control of the boiler control system. The boilers
may also operate in conjunction with the economiser; usually this means that
the economiser is operating at sea and one of the boilers is selected to act as
the water supplier and the steam collector for the economiser. The boiler
would operate if the economiser could not maintain steam pressure for any
reason.
The boiler control system controls the remote, manual and automatic
operations of one single-throat burner which is provided in the roof of the
boiler. This unit contains a programmable sequence control, which operates the
furnace purge, pilot burner and the automatic operation of the burner piston
valve. This is done by linking up with the boiler protective system and the
ACC. In addition, it transmits the automatic adjustment commands of
combustion air quantity and fuel oil quantity to the ACC for the start/stop of
the burner. Combustion control is at the heart of boiler operation because if
anything goes wrong with the boiler, its water supply or the combustion
system, fuel must be shut-off and that will prevent any problem becoming
more severe.
There are three boiler operating modes, one is the 18k mode (steam supply at
18kg-cm2), the second is the 7k mode (steam supply at 7kg/cm2) and the third
is the IGS mode (inert gas system in operation).
In port during cargo discharge the 18k mode would be selected but, at sea only
the 7k mode would normally be required with the oil fired boiler installation
providing support for the waste heat economiser. In some cases, intermittent
oil firing on the boiler may be needed to maintain steam pressure and the boiler
control panel would organise that. Selection of 18k mode or 7k mode is
executed by the changeover switch and selection of a particular mode auto-
matically changes the set point on the pressure indicator control (PIC).
Procedure for the Preparation of Boiler Control System
a) Turn on the power switches of the boiler control panel.
b) Check the action of each pilot lamp and buzzer using the buzzer
and lamp test switch on the control panel.
c) Supply air to all the control devices.
d) Reset the boiler interlock alarm.
e) Check that all alarm lamps are out.
Operating Method
There are three burner operating modes, AUTO (Automatic), MAN (Manual)
and HARD MAN (Hard Manual) mode. The burner is usually operated in the
AUTO mode and the MAN modes are only used in an emergency when the
AUTO mode cannot function. The HARD MAN mode allows for reposition-
ing of the burner switches and the MAN mode is for operating on manual.
Selection of Operating Modes
HARD MAN Mode
When operating in this mode, the operator must always be at the boiler and
able to monitor the situation and provide manual intervention at the control.
The following interlocks are effective:
Drum water level low-low
Flame monitor (pilot burner and main burner)
Operating Procedure
a) Check that the boiler and burner are in operating condition.
b) Start the fuel oil pump and the forced draught fan in the MAN
mode.
c) Turn the burner switch from the OFF position to the HARD MAN
position.
d) Set the fuel pressure controller and the air controller to the MAN
mode.
e) Purge the furnace. To do this the air controller should be manually
operated and the forced draught fan inlet vane should be fully
opened. The furnace must be purged for at least 3 minutes.
f) Check that the fuel temperature is within the required range.
g) Manually operate the air controller and the fuel oil pressure
controller and set the forced draught fan inlet vane and the fuel oil
control valve to the ignition open position.
h) Open the sub-door for the HARD MAN operating switches. Set
the pilot burner switch to the MANU ON position and ignite the
pilot burner. If the pilot burner has not ignited after 15 seconds the
pilot burner switch should be reset to AUTO and the process
started over again from item e) above, 'Purge the furnace'.
i) With the pilot burner burning correctly the main burner is ignited.
The fuel oil valve switch is set to MANU ON and the main burner
should ignite. If the main burner does not ignite after a period of
10 seconds the fuel oil valve switch should be reset to AUTO and
the procedure started over again from item 'e', above 'Purge the
furnace'.
j) With the main burner operating correctly the pilot burner switch
is reset to AUTO.
(Note ! When extinguishing the main burner the fuel oil valve switch must be
returned to AUTO.)
When burner purging is required, the burner purging switch must be used and
this must be set to MANU ON.
Fuel Oil Temperature Bypass
The fuel oil temperature by-pass switch is inside the sub-door. In this bypass
mode the starting interlock for fuel oil temperature low alarm is bypassed. It is
used when starting the boiler in the cold condition when steam is unavailable
for heating. When using 'A' grade heavy oil, the switch is set to BYPASS.
AUTO Mode
This is the mode which will normally be used. All operations, including the
commands for ignition and extinction, are operated automatically.
a) Set the fuel oil pumps, the forced draught fan and the controllers
to the AUTO mode.
b) Turn the burner switch from the OFF to the AUTO position.
When stopping this switch must be returned to the OFF position.
The following sequence of events must be accomplished for main burner
ignition.
a) When the burner switch is moved to the AUTO position the
program timer starts.
b) After a delay of 5 seconds the forced draught fan starts and the
atomising steam valve opens.
c) After a further 20 seconds the forced draught inlet vane starts to
move to the fully open position in order to purge the furnace. It
takes approximately 30 seconds to become fully open.
d) The purge timer (2P) commences when the burner switch is
moved to the AUTO position and the time set on this timer is 60
seconds. After the 60 seconds has elapsed, the forced draught fan
inlet vane starts closing gradually to the ignition position. At this
point the furnace will have been effectively purged.
e) The pilot burner is ignited 35 seconds after item 'd'.
f) When the flame of the pilot burner is detected by the flame eyes,
the electrical igniter stops sparking.
g) The main fuel oil valve opens 5 seconds after the pilot burner is
ignited.
h) The pilot burner is extinguished 15 seconds after it has been
ignited (item 'e').
i) The program timer stops at the lock-in position (graduation 85)
5 seconds after the pilot burner is extinguished.
j) If there is an ignition failure or a flame failure the burner control
goes into an extinction sequence.
k) The extinction sequence commences when the burner CUT
INTERLOCKS have actuated (following item 'j' above) or if the
burner switch is turned from the AUTO to the OFF position.
1) The program timer starts from the lock-in position.
m) The pilot burner is ignited 2 seconds after item 1) above.
n) The burner purge valve opens and the burner is purged for about
6 seconds. The burner is purged when the interlock is normal and
the pilot burner lights up.
o) The post purge period commences and the forced draught fan inlet
vane starts to open to its fully open position when the burner
completes it purge cycle.
p) After the set time (60 seconds) on the post-purge timer is
completed, the forced draught fan inlet vane starts closing to the
ignition position which takes about 30 seconds.
q) The forced draught fan stops after 30 minutes.
(Note ! If flame failure occurs during normal operation, it is important that the
cause of the failure is investigated before any attempt is made to restart the
boiler.)
Automatic Combustion Control
This system automatically regulates the fuel and air supply to the furnace in
order to maintain a preset steam pressure in the boiler. Regulation of the fuel
supply is accomplished by means of the air operated fuel control valve whilst
the air supply is controlled by means of the inlet vane of the forced draught fan.
Fuel supply is automatically cut off in the event of forced draught fan failure
or due to high or low water level in the boiler drum. The ACC system is
electro-pneumatically operated.
The automatic combustion control (ACC) system employed is of
a fuel oil pressure/air pressure measuring type.
The ACC is held at predetermined ignition position until the
burner is ignited.
After the burner is ignited the combustion rate is fixed at the
ignition position until the boiler pressure reaches the predeter-
mined pressure of 5 kg.cm2. This period is called 'steaming'.
When the steaming period is completed, the ACC system goes to
AUTO RUNNING and the combustion rate can be adjusted by the
system.
During the steaming period the combustion rate can be changed
by operating the fuel oil pressure controller in the MANU mode.
The air/fuel ratio can be changed by up to + 20% by altering the
air ratio dial. This dial would normally be set at the position 1.
MAN Mode.
This mode is selected to allow for manual starting of the boiler in order to see
that all stages are completed correctly. It is used when the boiler would
normally be operated automatically as a means of checking the start-up
procedure. The procedure is the same as for HARD MAN start but no switches
behind the HARD MAN sub-door are changed.
Feedwater Control.
This controller is of the two element type; both have proportional and integral
(P+I) control. It measures the steam flow rate and also the water level in the
boiler and adjusts the feedwater supply in line with changes in these values.
The P+I operation is performed when comparing signals from two separate
systems. One of the signals is generated by the difference between the water
level set and that detected in the steam drum of the boiler. The other is from
comparison between the detected steam flow rate from a steam flow
transmitter and the operating signal to the feedwater control valve. In ECON
(economiser) mode the water level change due to the ship's rolling and
pitching is accounted for by consideration of the moving average level in the
steam drum.

Master-Slave System.
The two boilers are independent units, but the control system is designed so
that they operate as a dedicated pair with one being the master boiler and the
other the slave. This means that the master boiler supplies the ship's steam
requirements until the demand exceeds its capacity and then the slave boiler
commences operation. The slave boiler will have been kept in a state of
readiness for such a situation and would have been at the same temperature as
the master boiler in order to avoid delays in wanning through.
a) The master boiler is controlled by actuation of the ON/OFF
switch and the pressure indicator so that the steam pressure of an
individual boiler will retain its set point. The actuation is executed
in the same way as the normal one boiler system.
b) When steam demand on the master boiler exceeds 80% of its
capacity, the slave boiler is switched on. It is switched off when
the steam demand is 30% of the total capacity of the two boilers.
The combustion rate for the slave boiler is the same as for the
master boiler, as the master boiler is exercising overall control.
c) In addition to the ON/OFF actuation of the slave boiler from the
master-slave controller, the slave boiler can also perform its own
ON-OFF actuation of combustion due to the pressure in the boiler.
The slave boiler retains overriding control of combustion due to
the pressure within the boiler and that pressure is the slave
boiler's own set pressure and is independent of the pressure
setting for the master boiler.
d) The low limiter actuates for 15 minutes after the slave boiler has
been started in order to prevent the ON/OFF hunting phenomenon
at the slave boiler.
e) The pressure in the slave boiler needs to exceed 11 kg-cm2 in
order for the master-slave configuration to operate.
f) In addition to the master-slave operation it is possible to select the
PARA mode where both boilers can be turned off independently.
In this case the boilers would be operating together each under its
own independent control and not as a master-slave pair.
Safety and Control System.
Incorporated in the safety and control system are operating functions, or sub-
systems, which react automatically to a change in condition outside of the pre-
set range. Failure of most sub-systems produces a visual alarm on the main
control panel and may also produce an audible alarm. In the majority of cases,
failure of a sub-system requires manual resetting of the cut-out before the sub-
system can be restarted. This provides protection for personnel on the ship and
for the boiler installation, as the reason for a sub-system failure can involve
more than that particular sub-system.


Inert Gas Topping-up Mode.
The inert gas system (IGS) topping-up mode is used in order to allow the boiler
to operate on a minimum load so that the IGS may function correctly. A
minimum boiler load of 25% is required so that the flue gases will contain no
more than 5% oxygen; the flue gas flow at minimum rate will be 10,300m3/h
at a temperature of 5°C. The following items will be interlocked, and hence not
operable, in this mode.
Boiler minimum load is limited to 30% or greater if dumping of steam
is operating.
The IGS running lamp is illuminated
Bypass of the FO burner auto stop
Steam supply valve to soot blowers is interlocked to FULL CLOSE

Boiler Alarm and Trips.
Description.

Emergency Mode.
The boilers may be operated in emergency mode when the burner sequencer is
inoperative.
a) Start the FD fan then fully open the FD fan inlet vane and perform
the furnace purge for 3 minutes.
b) Ensure that the FO temperature is at the specified level,
equivalent to 15cSt.
c) Set the FO control valve and FD fan inlet at IGNITION OPEN
positions respectively.
d) Light off the pilot burner with care and do not exceed 15 seconds
ignition time.


e) Ensure that the pilot burner has ignited and open the FO piston
valve to allow oil to the main burner.
f) Do not keep the FO piston valve open for longer than 10 seconds.
g) If the main burner fails to ignite, the furnace must be purged prior
to a repeat attempt at ignition.
(Note ! During an emergency operation a careful watch must be kept on the
boiler at all times.)
FO Temperature Bypass
When burning HFO during emergency mode this bypass must be operated.
Steam press. 7kg-cm2 mode (start-stop) 6.5 kg-cm2 - 9.5 kg-cm2
Slave boiler start enabled 11.0 kg-cm2
Slave boiler (start-stop) 12.6 kg-cm2 - 4.6 kg-cm2

 
 
Sootblowers
Auxiliary Boiler Sootblowers
No. of sets :

Two fitted to each boiler

Sootblowing has to be carried out at regular intervals to ensure that the heat
transfer surfaces are kept clear of deposits, as these retard heat transfer and can
constitute a fire hazard.
Two sootblowers are fitted to each boiler and should be operated daily when
boilers are in use, bearing in mind the position of the vessel and any local
legislation concerning pollution and clean air. They should be operated when
leaving port prior to shutting down the boiler. The sootblowers are fitted with
an air purge connection, the air being supplied from the discharge of the forced
draught fan. This purge or sealing air keeps the nozzles clear during boiler
operation and provides a seal at the air sealed wall boxes to prevent the escape
of boiler exhaust gas into the machinery space. Non-return valves prevent
steam from entering the air lines.
The sootblowers are only to be operated when the available steam pressure
exceeds 8 kg/cm2. An isolating valve, located in the steam line between the
sootblower steam supply valve (T25V) and the sootblower distribution line,
will only be opened by its associated pressure switch if the steam pressure
exceeds 8 kg/cm2.
Before operation, request permission from the bridge and notify the bridge on
completion.
Procedure for the Operation of the Auxiliary Boiler Sootblowers
a) The boiler should be on a minimum of 50% of full load and the
forced draught fan operating at a high rate during the sootblowing
period. The steam pressure must exceed 8 kg/cm2.
b) With the drain open slightly (No.l boiler valve T29V and No.2
boiler valve T28V), open the steam stop valve (T25V) to the
sootblower header.
c) When the pipeline is warmed sufficiently, shut the drain valve and
open the stop valve fully.
d) Operate the sootblower by turning the handwheel in a clockwise
direction. The sootblower cleans the boiler heating surfaces by
impacting steam from a row of nozzles set along the length of the
sootblower element. A cam and trigger arrangement, incorporat-
ed in the sootblower head, regulates the steam arc issuing from
the nozzles as the sootblower element rotates. This ensures
optimum cleaning of the tubes.
e) Operate the top sootblower first, followed by the bottom one. The
top blower should be operated again. The system is then shut
down and the drain valve opened.
WARNING
Do not operate the auxiliary boiler sootblowers during inert gas operations.

 
 

Emergency Operation and Putting Boiler out of Service

Emergency Operation
Low Water Level
A low water level, 140mm or more below the normal working level, will activate the visual and audible alarms (illumination of the alarm lamp on the control panel and sounding of the alarm buzzer).
Should the water level fall to 250mm or more below the normal working level, the fuel oil emergency trip valve will close, shutting off fuel from the boiler.
The feedwater valve and steam stop valve should be fully closed, the burner shut down completely and the forced draught fan stopped after purging the furnace.
Never attempt to supply feedwater to the boiler until the boiler has cooled sufficiently, as there is a danger of bringing comparatively cold feed into contact with hot surfaces.

When the boiler water level has been restored the boiler may be flashed up using the normal procedure.
Flame Failure
In case of flame failure, close the oil inlet valve and reduce air pressure to prevent over cooling the furnace.
Purge the furnace thoroughly before relighting the burner.
Always use the pilot burner for ignition, never attempt to relight the burner from the hot furnace refractory.
Evaporating Tube Failure
Serious tube failure where water level cannot be maintained.
a)  Shut off the oil supply to the boiler and if the tube failure results from low boiler water level, shut off the feed supply, close the feedwater valve and steam stop valve.
b)  If the tube failure results from a cause other than low water level, the fuel supply should be shut off but the feedwater supply should
be maintained in order to assist in the cooling down process.
When the boiler has cooled sufficiently, close the feed valve and steam stop valve and open the steam drum vent.
c)  In either case of tube failure, maintain the forced draught fan so that the air draft assists in carrying away the escaping steam.
Care must be taken to avoid damage to the refractory by an excessive air supply.
d)  Do not blow down the boiler unless the tube failure is so severe that personnel could be endangered.
When the boiler has cooled, the blowdown may be used to empty the boiler.
e)  When the boiler has cooled enough, an inspection should be carried out to assess the situation and carry out necessary repairs.
f)   If tube failure is not serious and the water level can readily be maintained, the boiler can be shut down in the normal manner.

The forced draft air supply should be maintained to carry away vapours generated by the leaking water and the water level
maintained during the cooling down period.
When boiler pressure has fallen to 2 kg/cm2, the steam drum vent valve boiler may be opened and the boiler blown down.
Putting the Boiler Out of Service
When putting a boiler out of service, the wet lay-up method is preferable, as it requires less preparation and it can be quickly returned to service.
These steps are taken if the ship is to be taken out of service for some time and are not part of normal operational routine.
Wet Lay-up
When the boiler is in the cooling down process following shutdown, appropriate quantities of boiler chemicals should be injected into the drum
using the boiler chemical injection device.
To ensure adequate protection of the boiler, follow the guidelines given by the chemical supplier.
The quantity of the chemicals required will depend upon the condition of the boiler water and a water test should be carried out prior to shutting down.
After dosing the boiler water should register pH of 12, (alkalinity 300 to 400 ppm) phosphoric acid about 50 ppm, and sodium sulphite 80 to 100 ppm.
The high alkalinity will ensure adequate protection of the boiler.
When returning the boiler to service the chemical concentrations should be returned to normal levels and this means blowing down the boiler and filling with untreated make-up feed.
a)  When the pressure is approaching atmospheric pressure, open the steam drum air vent valve.
b)  When the pressure is off the boiler, supply distilled water until it issues from the vent valve, then close the vent valve.
c)  Put a hydrostatic pressure of 3.5 to 5kg/cm2 on the boiler.
Hold this pressure until the boiler has cooled to ambient temperature.
Bleed the boiler using the vent valve to be sure all the air is out.

Maintain a hydrostatic pressure of 2 to 3.5 kg/cm2 on the boiler.
Take a periodic boiler water sample and replenish any depleted chemicals.

Maintaining Boiler in Warm Condition
At sea, with one boiler being circulated through the waste heat economiser, the standby boiler should be maintained in a warm condition by supplying steam to the heating element in the bottom drum.
This is done by closing the heating coil drain valve and opening the inlet and outlet valves.
The boiler pressure should be maintained at 0.5 kg/cm2 or above.
When the heating element is not in use, the inlet/outlet valves are closed and the drain left open.
In port with the economiser shut down, the standby boiler is maintained at 2kg/cm2 or above by switching the burner on and off. Do not use the bottom drum heater.
Dry Lay-up
This should only be undertaken if a wet lay-up cannot be performed.
a)  Whilst the boiler remains warm, drain it of all water and ensure that all headers are dry.
b)  Remove the end piece of the waterwall lower header to check that no water remains.
c)  Provide some dry heat, electric heaters preferably, in the furnace to promote internal drying.
d)  When the boiler is completely dry, put some quick lime or calcium chloride in a shallow dish for placement in the drum and
header then close the end plate and manhole doors.
Check the moisture absorbent chemicals every week initially and replenish as required.
e) Cover the funnel outlet and close the air inlet to the furnace.

Marine Boiler Operation Construction


Boilers and Steam Systems
General Description
The steam generating plant consists of two auxiliary boilers and one exhaust
gas economises Steam is required at sea for fuel, domestic water and cargo
slop tank heating purposes. In port steam is used additionally for driving the
power turbines of the cargo pumps and No. 1 water ballast pump. The steam
demand of the plant, in port, is served by the boilers. At sea, steam demand is
met by circulating boiler water from one of the auxiliary boilers through the
exhaust gas economiser, by one of the boiler water circulating pumps. The
auxiliary boiler acts as a receiver for the steam generated by the economiser.
The economiser is arranged in the main engine exhaust gas uptake to take
waste heat from the main engine exhaust. An auxiliary boiler may be required
at sea in low temperature areas, as well as reduced power operation of the main
engine, such as during manoeuvring or slow steaming on passage when there
will be insufficient waste heat to generate the required steam.
Auxiliary Boiler
No. of sets: 2
Maker: Hyundai Heavy Industries Ltd
Model: HMT-50
Type: Top fired rectangular water tube marine boiler
Evaporation: 50,000 kg/h
Steam Condition: 18 kg/cm2 saturated steam.
Fuel Oil: HFO up to 700 cSt at 50°C
Safety Valve Setting: 20 kg/cm2
Fuel Oil Consumption: 3,850 kg/h at 100% evaporation
Boiler Associated Equipment
Equipment
Combustion Control Electronic/Air Operated
Feedwater Regulator Electronic/Air Operated
Remote Water Level Gauge
Drum Level Safety System
Steam Jet Oil Burner
Water Level Gauge - Reflex Type
Safety Valve - Full Bore Type
Chemical Dosing Unit
FDFan
FO Pump
FO Heater
Description
General Construction
The boiler is of the two drum rectangular type, with a membrane furnace water
wall connecting steam and water drums.
The furnace consists of gas-tight membrane walls, the downcomer pipes are located outside of the furnace.
The fuel burner unit and associated combustion air inlet, is located in the roof of the furnace with the burner firing downwards using a steam assisted pressure jet burner.
At the furnace bottom, a refractory protects the furnace bottom from the combustion flame.
Combustion gases flow downwards and through the lower part of the division tube wall and the lower section of the generating tube
bank which connect the steam and water drums.
The gases then flow upwards on a return path through the upper part of the generating tube bank to the flue gas box at the top of the boiler.
Radiant heat generates steam in the membrane furnace water wall tubes.
The membrane wall has access doors to allow for furnace inspection and cleaning.
The boiler structure is rigid enough to withstand rolling, pitching and shock loading of the ship operating in a seaway.
The boiler is supported at the water drum and the water wall lower headers, and there are no rigid connections at any other points in order to allow for thermal expansion.
Furnace
Closely spaced water wall tubes of 76.2mm outside diameter, form the membrane walls at the side, roof, except for burner opening, rear, and front of the furnace.
This construction is in order to increase the radiant heat absorption in the furnace and to make it strong enough to withstand vibration.
The furnace is made completely gas-tight by the welded water wall construction.
Situated at the top and bottom of the front and rear walls are water wall headers.
Water enters the bottom headers and rises through the tubes to the top headers due to natural convection.
As the water rises, it is heated until its saturation temperature is reached and it then begins evaporating.
This water- steam mixture is passed to the steam drum via the top headers.
Front and rear water wall tubes connect to steam and water headers at the top and bottom respectively; one end of each top header connects with the steam drum and one end of each bottom header connects with the water drum.
The roof, side and bottom water wall tubes are directly connected to the water and steam drums.
The steam generating bank of tubes, connecting steam and water drums, is located within the furnace.
Boiler Casing
As the furnace of the boiler is made completely gas-tight by the adoption of welded membrane water wall construction, no casing or refractory is required to contain the combustion gases.
Mineral wool insulation is provided on the outer surface of the furnace water walls and this is covered by corrugated galvanised sheets to reduced heat transfer.
The maximum temperature on the casing surface will not exceed 60°C.
Steam Drum and Fittings
The steam and water drums are fabricated using boiler steel plate of all welded construction.
The steam drum has a horizontal perforated baffle plate covering the entire water surface in order to prevent droplets of water rising to the upper part of the steam drum.
A steam separator is provided to completely remove the moisture.
The feedwater pipe enters the steam drum at the rear of the boiler and is attached to an internal perforated feed pipe which extends to the front of the steam drum.
This ensures that there is complete mixing of incoming feed with the existing boiler water and an equalising of temperatures.
The chemical feedwater treatment pipe attaches to the internal feedwater pipe and this also ensures that there is complete mixing of the chemicals before the water reaches the downcomers.
The open ended surface blow off internal pipe extends to the surface of the steam drum to ensure that only floating solids on the water
surface are discharged through this scum blowdown line.
The boiler blowdown connection is fitted to the lower part of the water drum.
Sootblower - Rotary Type
Operating Procedures
Procedure for Preparing the Boiler for Service
The following steps should be taken before attempting to flash up the boiler.
a)  All foreign materials must be removed from internal pressure parts.
b)  All gas side-heating surfaces must be clean and all refractory be in good condition.
c)  The furnace bottom and the burner wind box must been cleaned of oil and other debris.
d)  All personnel not involved must remain clear of the boiler.
e)  All manhole covers must be securely tightened.
f)   Inspect safety valves and ensure that gags have been removed and easing levers are in good condition.
g)  Open root valves for all instruments and controls connected to the boiler and check that they work as intended.
h) Open the vent valve of the steam drum.
i) Open all pressure gauge valves and check to ensure that all valves on the pressure gauge piping are open.
j) Check and close all blow-off valves and drain valves.
k) Fill the boiler until water level appears 25 to 50mm high in the gauge glasses.
Allow for swell in level after firing.
1) Check the operation of gauge glasses.
Remote reading instruments will not work correctly until the boiler is under pressure and so they must not be relied upon.
Raising Pressure With No Steam Available from the Other Boiler or Economiser
With the boiler water at the correct level and other checks made as above:
a) Set up the fuel system for diesel oil and circulate the fuel until all heavy fuel has been discharged from the fuel lines.
Ideally the fuel system should have been flushed through with diesel oil prior to the previous shutdown.
b)  Set the burner for air atomising, using an air pressure of 5 kg/cm2 and fuel pressure of 3 kg/cm2.
Purge the furnace with the forced draught fan for one minute with vanes fully open.
c)  Reduce the air pressure at the windbox to between 10 and 20mm WG and close recirculating valve.
d)  Light the burner using the pilot burner and adjust air and fuel pressure to ensure stabilised combustion by using the furnace
observation port and smoke indicator.
e)  When raising the pressure, keep the burner firing for 5 minutes and out of service for 15 minutes repeatedly at the lowest fuel oil
pressure (2.5kg/cm2) for one hour.
Again, repeatedly light and shut down the burner to raise pressure as recommended on the pressure raising curve supplied by the manufacturer. A guideline would be to aim for lkg/cm2 after 2 hours firing, 5kg/cm2 after 2.75 hours firing and 12 kg/cm2 after 3.25 hours firing.
f)   When the drum pressure has risen to about 2 kg/cm2, close the drum vent valve.
g)  Drain and warm through all steam supply lines to ancillary equipment before putting the boiler on load.
h) Supply steam to one of the HFO service tanks.
When the tank is of sufficient temperature to be pumped by the HFO pump, supply steam to the HFO heater and prepare to change over from DO to HFO firing.
The HFO must be thoroughly circulated through the system to ensure it is at the correct temperature for good combustion.
When firing on HFO, check the combustion and adjust the fuel and air as required, then continue pressure raising.
(Note ! Caution must be exercised when operating with diesel oil due to its lower flash point. Diesel oil must not be heated above 40°C and there is a greater risk of leakage compared with HFO.)
i) At working pressure, switch to automatic operation.

Raising Pressure with Steam Available from the Other Boiler or Economiser
a)  Start the forced draught fan, open the inlet vanes and purge the furnace.
b)  Ensure that the HFO system is correctly heated then start the HFO burning pump and circulate oil through the heater and burner
manifold, open the recirculating valve and discharge the cold HFO in the line.
(Note ! At normal sea going condition, the boiler fuel system should be continually circulating heated HFO.)
c)  Reduce the air pressure at the windbox to between 10 and 20mmWG.
d)  Close the recirculating valve.
e)  Light the burner and adjust the air and fuel pressure to ensure stabilised combustion, using the furnace observation port and
smoke indicator.
Boiler pressure must be raised gradually over a period of hours in accordance with the manufacturer's instructions.
The recommendations are the same as in item e) in the section; Raising Pressure With No Steam Available
f)   When the drum pressure has risen to about 2 kg/cm2, close the drum vent valve.
g)  Drain and warm through all steam supply lines to ancillary equipment before putting the boiler on load.
Shutting Down
a)  Operate sootblowers before shutting down the boiler whenever possible.
b)  Shut down the burner.
c)  Continue operation of the forced draught fan for a short while after shutting down, keeping an air pressure of 150mm WG at burner inlet and purge the furnace of combustible gases.
d)  Maintain the water level visible at about 50mm in the gauge glass and when the boiler is closed raise the water level 70mm to 120mm above the normal water level.
e)  Open the drum vent valve when the boiler pressure reaches about 2 kg/cm2.
f)   Change the fuel system to diesel oil and circulate back to the tank.
(Note ! If steam is to remain available from the other boiler or economiser, the boiler HFO system should remain in use and there is no need to change to diesel oil.)
g)  When fuel oil has been purged, shut down the fuel system.
After the boiler has been shut down for 4 hours the forced draught fan may be used to assist cooling down should immediate access be required. However, to avoid the risk of damage to refractory, allow the boiler to cool down under natural means if possible.
! CAUTION
Do not attempt to cool down the boiler by blowing down or by filling with cold water.

Wednesday, June 22, 2011

Boiler and Control System


Introduction

Economizers are heat exchangers which are fitted in a boiler to increase the efficiency of the boiler. This is done by extracting the heat from the exiting gas and using it to heat the feed water entering the boiler.

To obtain an acceptable degree of efficiency and reduce fuel consumption as much as possible by introducing further heat recovery surface so that the gas temperature at the funnel may be as low as practicable, the gas temperature leaving a boiler cannot be reduced much below 30oC above the saturation temperature. In radiant types a much higher exit gas temperature is usually found. To carry out this further heat exchange, surfaces such as economizers and air heaters are commonly used.
In many radiant boiler types, economizers are also found arranged integrally within the boiler unit. In this location they consist of a number of multi-loop elements of plain tubes connected at their ends to inlet and outlet headers.
Since are situated in a hot gas temperature zone and are required to perform a considerable heat exchange duty, a portion of the water pumped through them may be converted into steam. These steaming economizers are arranged so that water enters the lower header and the steam and water mixture leaves from the top header to the steam drum where the steam and water separate.
Economizers are used externally to boilers for further heat recovery. Economizers are found in the cooler gas zone and are fed with water temperatures around 116oC or 185oC depending upon whether the feed cycle includes high pressure feed heaters after the de-aerator.
BOILER WITH THE ECONOMIZER
INSPECTION ON GAS SIDE:
Before going into economizer inspection, first inspect the gas side of the boiler. It gives you a clear picture of boiler working condition and the efficiency of heat transfer surfaces.
1.      Check exterior of drums for sign of tube roll, leakage, corrosion, soot erosion and overheating.
2.      Condition of outside drum insulation.
3.      Drum seals for signs of air leakage.
4.      Inspect drum support for cracks and expansion clearance.
5.      Check all the blow-down connection for expansion and flexibility of support.
6.      Inspect all piping and valves for leaks.
7.      Visually check water wall tubes and fins for cracks.
8.      Check exterior of all tubes for corrosion, carbon-build up, erosion, blisters and sagging.
9.      Inspect tubes at soot blower for sign of steam impingement.
10.  Check header seals for signs of air leakage.
11.  Examine exterior of headers for corrosion, erosion, thermal cracking and condition of insulation.
12.  Condition of refractory.
13.  Around the burner assembly check refractory, tube condition and accumulation of soot or carbon.
14.  Check soot blowers for distortion, worn bearings, rubbing of tubes, condition of nozzle cracks, freedom of movement and effective lubrication.
INSPECTION ON ECONOMIZER:
1.      The major problem at the economizer section is low temperature corrosion and problems from gas side deposits.
2.      Sliding and leaky expansion joints at the casing may allow accumulation of soot with severe acid attack.
3.      Inspection of tubes bends by opening the inspection covers needs to be carried out to check these.
4.      Uptake area may show cracked expansion bellows sign of acid corrosion.
General cleanliness of these areas indicates the combustion performance in boiler.
·   BOILER INSPECTION
·   ECONOMISER
Design and Setting of the Marine Boiler Safety Valve
CATEGORY:Safety valves are fitted to protect the boiler from the effect of over pressure. At least two safety valves are fitted to each boiler steam drum, but if there is a super heater, another safety valve should be fitted on it.
Introduction: Marine Boiler Safety Valves
The pressure setting of the superheater safety valve should be less that the designed pressure of the boiler, i.e. less than that of the steam drum safety valve, to ensure flow of steam through the superheater under blow off conditions. The pressure setting of one steam drum safety valve should be same as the design pressure of the boiler. The pressure setting of another safety valve should be 2-3 % more than the designed pressure of the boiler.
Classification of Boiler Safety Valves
There are three types of safety valves used in marine boilers:
1.      Improved high lift safety valve
2.      Full lift safety valve
3.      Full bore safety valve
Boiler Safety Valve
Improved High Lift Safety Valve:
1.      Wingless valve improves steam flow and reduces risk of seizure.
2.      Waste steam pressure acting on the piston gives increasing valve lift.
3.      Special shaped seat deflects steam towards lip on valve and increases valve lift.
4.      The valve lifts, the force to compress the spring increases, so the higher valve lifts the greater the increasing in boiler pressure.
5.      Waste steam pressure keeps cylinder in place while piston moves, also by having a floating cylinder, seizure risk is reduced.
6.      A lip is placed around the valve seat so that when the valve lid lifts, escaping steam is trapped in the annular space around the valve face, the resultant build–up of pressure acting upon the greater valve lid area causes the valve to lift sharply. This arrangement gives another advantage to close the valve cleanly and sharply with very little blow down effect.
7.      The improved high lift safety valve makes use of waste steam pressure to increase the valve lift; this is done by allowing the pressure to act upon the lower spring carrier which fits within a floating ring so forming in effect a piston. The pressure acts upon this piston causing it to move up, helping to compress the spring and so increasing the valve lift.
8.      Loose fitting key or pad lock is provided to ensure proper closing of valve.
9.      Loose pin is provided to secure valve lid and allow thermal expansion.
10.  Adjustment of the valve is carried out by means of a compression nut screwing down on to the top spring plate.
11.  A compression ring is fitted after the final adjustment to ensure no further movement takes place.
12.  A cap is then fitted over the compression nut and the top of the valve spindle, a cotter is passed through and padlocked to prevent tampering by unauthorized person.
13.  Clearance between this cap, the valve spindle and cotter are such as to prevent the valve being held down externally.
14.  Easing gear is fitted so that in the event of an emergency the valve can be opened by hand to a full lift ¼ D to release the boiler pressure.
Valve Area: As = A × (1 + Ts / 555)
·         As- Aggregate area through the seating of valve (mm2) for superheated steam.
·         A-Aggregate area through the seating of valve (mm2) for saturated steam.
·         Ts- Degree of superheated steam in oC.
15. Valve Area (As) greater than (A) due to specific volume of steam increases with increases of temperature at constant pressure and more escape area is required to avoid accumulation of pressure.
16. The area of valve chest must be at least (1/2) A.
17. The waste steam pipe and steam passage must be at least 1.1× A.
Manual Hand Trying of Boiler Safety Relief Valve:
To check the proper working condition of the boiler safety valve we carry out the “Hand trying out the Boiler Safety valve” at regular intervals. The safety valve is provided with the easing gear which manually lifts the safety valve and releases the excess pressure in the boiler. When the easing gear is pulled, the valve will be opened by hand to a full lift of ¼ D to release the boiler pressure. Before carrying out the process the boiler safety valve has to be drained.

Boiler Safety Valve Drain:
Draining of the boiler safety valve is necessary as to prevent any build-up of water in the pipe line causing head of water to form over the valve lid so increasing the blow off pressure. So at regular intervals the boiler safety valve should be drained.
1.      Drain pipe must be fitted to the lowest part of the valve chest on the discharge side of the valve.
2.      The pipe should be led clear of the boiler.
3.      The pipe must have no valve or cock fitted through its length.
4.      The open drain of the pipe should be regularly checked.
5.      If the pipe becomes chocked, there is possibility of overloading the valve due to hydraulic head, or damage due to water hammer.
6.      The waste steam pipe of the boiler safety valve should be well secured so that no load of the pipe is on the safety valve, which can be the cause of additional stress on the valve.
Pressure Setting of the Boiler Safety Valve:
If it is found that the boiler safety relief valve is not lifting at the designed lifting pressure, manual pressure setting of the boiler safety valve has to be done for the proper and safe operation of the boiler. The adjustment can be carried out on this type of valve to give the desired discharge and blow down characteristic.
1.      Safety valve pressure setting can be done from high to low pressure or vice versa.
2.      Take necessary personal safety precaution and arrange tools i.e. gagging tool and master gauges.
3.      Slowly raise the boiler pressure and blow off the safety valves manually few times for thermal expansion and to reduce the thermal stress on the valves.
4.      Then screw down all the safety valves higher than the setting pressure at which you are going to set.
5.      Raise the boiler steam pressure 2-3 % more than the designed pressure of the boiler, then stop firing and unscrew the first valve slowly, when it blows off at 2-3 % more than the designed pressure then note this opening and closing pressure of the valve and finally gag it.
6.      Raise the boiler pressure at the designed pressure of the boiler and unscrew the 2nd valve, when it blows off at designed pressure then note this opening pressure and check the closing pressure also. Recheck the setting pressure and gag the valve.
7.      Then set the superheater safety valve lower than the designed pressure of the boiler in same procedure.
8.      Finally take out the gagging tools. Pressure setting should be done in presence of surveyor
·   SAFETY VALVE
Boiler Inspection or Survey Carried Out at Regular Intervals

CATEGORY:
The boiler is vital equipment on ships. It is used as main propulsion (in steam ships) and for auxiliary heating in other ships. It is very sensitive and dangerous equipment, where there should be regular inspections and surveys carried out to avoid accidents and outages.
BOILER INSPECTION
Introduction
Normally boiler inspection will be carried out onboard the ship by a port state control and during the dry dock. They are used to carry out the inspection and see the working condition of the boiler. During the inspection they will conduct an in-depth analysis of the boiler condition considering various factors to find the working condition of the boiler. If necessary they will replace damaged parts of the boiler needed for continued safe operation.
NEED FOR BOILER SURVEY OR INSPECTION
1.      Boilers are inspected to maintain the Class requirement.
2.      Regular internal inspection and external examination during such survey constitute the preventive maintenance schedule the boiler goes through to have a safe working condition.
FREQUENCY OF BOILER SURVEY
1.      Water tube high pressure boilers are surveyed at two year intervals.
2.      All other boilers, including exhaust gas boilers, are surveyed at two yearly intervals until they are eight years old and then surveyed annually.
PLANNING FOR BOILER SURVEY
1.      Confirm time available, manpower, and time required.
2.      Check before shutting down boiler.
3.      Check for spares e.g. manhole door joints, gauge glass, packing and steam joints.
4.      Check the tools required e.g. gagging tool, torque spanner, rope, chain block etc.
5.      Check manual for special instruction and past records.
6.      Steam requirement for the next port should be considered e.g. Tankers require steam in discharged Port.
7.      Briefing to other engineers of work involved.
SHUTTING DOWN THE BOILER FOR INSPECTION
Before inspection is to be carried out, the boiler which is firing should be shut down. These are the steps to be followed before shutting down the boiler for inspection.
1.      Inform the chief engineer and inform the duty officer in the bridge.
2.      Change over M/E, A/E, and Boiler to diesel oil.
3.      Top up diesel oil service tank, stop heavy oil and lube oil purifiers.
4.      Stop all tank and tracing steam heating and carry out soot blowing.
5.      Change over from automation to manual firing of boiler.
6.      Stop the firing of the boiler and purge boiler for three to five minutes.
7.      Switch off power and off the circuit breaker for forced draught fan, FO pump, feed pump, and combustion control panel. Hang necessary notices.
8.      Shut main steam-stop valve and shut all fuel valves to boiler.
9.      Let the boiler cool down, do not blow down now.
10.  When the boiler pressure is about 4 bars, carry out blow down.
11.  When boiler pressure is slightly higher than atmospheric pressure, open the vent cock to prevent formation of vacuum.
12.  Let the boiler cool down.
13.  Once sufficient cooled, open top manhole door first with all safety precaution.
14.  Mark the nut on the top manhole, slacken the dog-nut, and secure it with a rope.
15.  Knock the manhole door gently, but do not open it as it may contain steam or hot water.
16.  Conform nothing coming out; open the door fully with the help of securing rope.
17.  Do not open immediately open the bottom door, since the boiler is still hot and if opened relatively cool current of air will pass through the boiler causing a thermal shock.
18.  Allow further cool down before opening bottom manhole door.
19.  Open the bottom manhole door with the same precautions and open the furnace side door also.
20.  Ventilate foe period of 12 to 24 hours.
21.  Then check for oxygen, flammable vapour, and toxic gasses.
22.  If it is safe, prepare for entry.
PREPARATION FOR ENTRY
These are the steps to be carried out before entering the boiler for inspection.
1.      Prepare a long rope, wooden plank oxygen analyzer, safety hand lamp, and safety torch attached with rope.
2.      Get a pouch to carry tools and keep track of the number of tools to be brought into boiler.
3.      Personnel safety protection wear, e.g. helmet, safety shoes, hand gloves, etc.
4.      No extra instruments to be brought in and clear pocket contents as it may fall into boiler.
5.      Keep an emergency breathing apparatus ready.
6.      Remain in communication and ensure proper lighting.
7.      Check boiler internals before making an entry, e.g. foothold and handhold.
·   BOILER SURVEY
Inspection Carried Out In Boiler Superheater and In Steam Drum

SUPER HEATERS
The superheater is a device which converts saturated steam or wet steam to dry steam, and it is used in driving the lager turbines in the marine propulsion system. In the superheating process the temperature of the steam is only raised, keeping the pressure at a constant level.
Superheating process can be done by three methods:
1.      Radiant superheating: In this type, the superheating tubes are placed directly in the combustion chamber.
2.      Convention superheating: In this type of super heaters the superheating tubes are placed outside the combustion chamber on the path of the hot gases.
3.      Separately fired: In this type the superheater tubes are placed in the separate combustion chamber outside the boiler. This is separately fired to maintain the required temperature of the superheated steam outlet.
In the superheater zone the products of combustion were still at a high temperature and deposits from impurities in the fuel condensed out on the tubes, reducing heat transfer and steam temperature. Eventually gas passages between the tubes would become so badly blocked that the forced draught fans would be unable to supply sufficient air to the burners, combustion become impaired and the fouling condition accelerated. Sodium and vanadium compounds present in the deposits proved very corrosive to superheater tube causing frequent repeated failure. Due to the fouled conditions there was a loss of efficiency and expensive time consuming cleaning routines were required.
Inspection on Superheater
1.      Internal and external examination of heaters.
2.      Thermal crack at the headers due to high stresses set up across the thick welded section is possible.
3.      Super heater safety valve and stop valve.
4.      Super heater drains and vents valves and manhole openings to check.
5.      Efficiency of the “screen” plates to ascertain –these protect headers from direct heat of furnace.
6.      Superheater tubes are also prone to high temperature creep failures and thermal fatigue cracking sudden quenching can cause fatigue failure.
7.      Check for deposit accumulation in header.
8.      Drain valve from headers to examine.
Super Heater Walk-In Spaces:
1.      Supports of horizontal super heater tubes to check for burning away and leave the unit unsupported and cause drainage problems.
2.      Super heater support tubes may also crack due to effect of bending fatigue stresses due to misalignment of tubes in the tube holes.
3.      Build-up of deposit is most troublesome defect in super heater. These may result in high furnace pressure, loss of super heater and poor combustion.
4.      Special attention and suspicion to be reserved for tubes through which there still exist gas paths as they operate under excessive metal temperature.
5.      Oxide scaling inside or outside may cause tube failure and worst case hydrogen fire when iron burns in steam at above 700*C in exothermic reaction, and destroys all boiler, economizer and air heater.
Now you have a clear picture on the various inspections carried out on the marine boiler parts for the safe and efficient working of the boiler.
·         BOILER INSPECTION
·         STEAM DRUM
·         SUPERHEATERS
·         SUPERHEATERS
·     Inspection carried out in Boiler Superheater and in Steam Dr
Learn how inspection is carried out in boiler steam drum, headers and super-heater tubes.
INTRODUCTION
The steam drum is one of the important parts of the boiler which acts as the reservoir for the steam generated and for water required for the boiler. Mainly all the boiler mountings are mounted on the steam drum and it should possess sufficient strength to withstand the high temperature and pressure of the steam generated.
As before, in inspecting the generating tubes, headers, and superheater tubes of the boiler, the inspection has to be carried out in the boiler steam drum.
Check the steam drum for corrosion, scaling, and pitting:
1.      Manhole seats and surface condition.
2.      Condition of all feed, chemical feed, blow down lines and inside pressure parts or chocking, security, and leaks.
3.      Check for freedom of expansion of drums and headers.
4.      Inspect tubes for corrosion, excessive deposits, flare-cracking, and pitting.
5.      Inspect hand-hole plates and stud threads.
6.      Make a complete waterside examination and check for scale build up as necessary.
7.      Measure thickness of scales by using commercially available gauges.
OUTSIDE STEAM DRUM:
1.      All internal (removed from drum) checked and tested.
2.      Feed regulator, feed check valve, water gauge fittings, and drum safety valves examined. Attention to securing arrangement of seats in valves covers to valve chest to drum nozzles.
3.      Welded connection of drum to casing to check for any possible damage creating gas leakages.
4.      Areas of drum not protected by tubes from heat radiation and shielded refractory. Thermal cracking of the refractory material to be checked.
STEAM DRUM
HEADERS
Boiler headers are the water feeders to the generating tubes in boiler. The headers are connected in between the steam drum and the water drum. Normally the water from the water drum enters the main headers from there and many generating tubes are connected where the steam is generated.
Rear and Side Wall Headers:
1.      Sufficient doors or handhole plugs to remove for assessment of internal condition of headers and tubes.
2.      Check for pitting and corrosion of headers, rear walls, floors, roofs, and side wall tubes.
3.      Check for casing defects for possible gas or air leakage.
Bottom Header:
This contains the furnace tubes and the down comer tubes. A number of handhole doors is provided for internal inspection and repair to the tubes.
·         Inspection for deposits of sludge must be carried out during the survey.
·         Regular blowing down from this header will be necessary to keep it clear of sludge deposits.
·   BOILER INSPECTION
·   STEAM DRUM
Repairs in Marine Boilers

CATEGORY:
This article discusses the general repairs needed in the marine boiler and how to repair them directly on board. Some common repairs are leaking of tubes in both smoke tube and water tube boilers, busting of tubes, and leakages in the manhole joints.
Introduction
Some of the common repair work carried out on the marine boiler while on board the ship is plugging of the tubes and replacing the leaky manhole joints. Other major repairs like the renewal of the damaged tubes and furnace rebuilding must be carried out in the dry dock. The plugging of the boiler leaky tube is a temporary repair which must be carried out in order to fire the boiler. Whatever the situation, and in any condition the boiler must run to supply the working steam.
When the gasket becomes damaged or gets old, smoke starts to come out of the boiler in the case of the water tube boiler. In the smoke tube boiler, the water starts to leak outside the boiler. This must be repaired on board by replacing the leaky manhole joints.
Replacement of a Leaky Manhole Joint
1.      Maintain proper spigot clearance- 1.5 mm to position the door centrally for evenly loading the gasket.
2.      Never use an old gasket.
3.      Do not over strain the door studs, which may stretch.
4.      Pull-up studs by re-tightening the nut after steam rising or warming up.
5.      Avoid causing damage to door by holding it by a rope and gently lowering it inside or taking it out.
6.      Mark the dogs and nuts to fit back correctly in the same door.
7.      Check for wear and tear on the studs and nuts.
8.      Carefully check the matting/ landing surface for corrosion and erosion on the door and boiler before reassembling.
Repairs in Smoke Tube Boilers
Procedure for Plugging of a Damaged / Busted Smoke Tube:
1.      Hydrostatic testing to mark the leaky tubes.
2.      Cut the tubes on one end and clear of the tube plate. At the other end the tube is collapsed inside the tube plate.
3.      Pull out the tube from the collapsed end.
4.      Insert a short tube into the tube plate and weld it in place.
5.      Lap the spare tapered plugs on both stud ends in the tube plates.
6.      Insert the tube plugs and tack weld it.
7.      Alternatively, the plugs can be held in place by a long steel bar threaded and bolted at both ends.
8.      Hydrostatic pressure test to confirm no leaks.
9.      Flush up the boiler and re-inspect the plugs for leaks under full steam pressure.
Temporary Repairing Procedure to Rectify the Leakage in Smoke Tube:
1.      Stop the burner, allow the boiler to cool and remove the soot.
2.      Allow boiler to depressurize, and open the blow down valve to drain the boiler.
3.      Enter the boiler flue box and cut a hole in the side of the relevant smoke tube.
4.      Clean the rim of the smoke tube with a wire brush.
5.      Cut a circular plate (15 mm thick) of the same diameter as the smoke tube and chamfer the top edge to 30 degrees by grinding.
6.      Fit the plate into the top of the smoke tube and weld it in position as shown.
7.      Enter the boiler furnace and cut a similar hole in this end of the relevant smoke tube.
8.      Repeat steps 4 to 6 for lower plate.
9.      Refill boiler and check for leaks before start-up.
10.  Start-up boiler and check for leaks when pressurized.
Note: Any temporary repair to smoke tubes or boiler tubes should receive more permanent attention as soon as conveniently possible.
Repairs in Water Tube Boiler
Instruction for Plugging / Repair of Water Tube Boiler & Economizer:
1.      In case of tube failure, steam pressure has to be removed and the oil burner dismantled.
2.      If the leakage is readily visible from the burner hole, the boiler can be emptied and repairs commence.
3.      Otherwise, the boiler is given pressure by means of the feed pump. The position of the leakage will be indicated by the water flow.
4.      This flow may not be visible from the burner hole. If it is not visible, remove the inspection door and enter the furnace. If the tube failure is still not found, then enter the generating tube section. From here the bottom of the membrane walls and generating tubes can be inspected for leakage.
5.      If the leakage has resulted from the membrane walls or generating tube, the inspection door at the smoke connection pipe must be removed, and the generating tube/ membrane tube in which the failure has occurred is pointed out.
6.      The leakage may also result from economizer.
7.      By removing the inspection door at the bottom of the economizer, it can be determined which uptake has caused the leakage?
8.      If necessary other inspection doors should be removed to point out the damage register.
9.      When a damaged tube or convection register has been removed, and the remaining tube studs have been repaired/ plugged a new tube or register should be mounted as soon as possible.
10.  Operation for longer periods with one or more registers missing involves the risk of further damage to the boiler due to increasing heat leads on the parts next to the ones removed.
REPAIR IN MARINE BOILER
Scope of Inspection of a Ship’s Boiler
The boiler is one of the items of equipment on a ship which continuously keeps on running during sailing and in port. As it is running continuously, it has to be cleaned and inspected to check the condition of all internal working parts at regular intervals.
SCOPE OF INSPECTION
The scope of inspection is to clean the boiler’s internal surfaces and to check for corrosion and scale formation in the boiler. As the boiler normally runs continuously, there are few chances to open the boiler. Thus, during the inspection all the important checks will be carried out and it will be made sure that the boiler will safely work without any problems until the next inspection. Routine inspection is important because salt formation and scaling inside the boiler tubes will reduce the heat transfer rate and ultimately damage the tubes due to overheating.
1.      The inspection should include finding reasons for any abnormality found and should also ensure that any repair carried out does not affect that safe working order of the boiler.
2.      A complete inspection means full internal and external examination of all parts of the boiler and accessories such as super-heaters, air heaters, and all mountings.
3.      The examination may lead the inspector to require hydraulic testing of pressure parts or thickness gauging of plate or tubs that appear to be checked for good working condition.
The Inspection is not completed until the boiler has been examined under steam and the following items dealt with:
a) Pressure gauge checking against a test gauge.
b) Testing of water level indicators and protective devices.
c) Safety valves adjusted under steam to blow off at the required pressures.
d) The oil fuel burning system examined.
e) Testing of remote control gear for fuel shut off valves.
For a gas fired boiler, the chief engineer floats the safety valve at sea at the first opportunity. Survey record is not assigned until a statement is received from chief engineer about the pressure at which the safety valves were set.
Inspection Consists Of:
a) Examination of the items.
b) Statement whether a problem / defect exist.
c) Determining the cause of problem.
d) Define the repair and whether temporary / permanent.
The Main Benefits of Doing Inspection:
By doing the inspection, we are manually cleaning the boiler scales and chemical cleaning of the salt formation in the boiler parts and making the boiler safe for operation. It also helps in checking the redundancy of the stand-by boiler. During the inspection the newly signed in crew members and the ship’s engineer will also have a chance to see the internal parts of boiler.
1.      Boiler must be sufficiently cleaned and dried to make a thorough examination possible.
2.      Boiler should be manually wire-brushed to clean the internal surfaces.
3.      In case of difficulty in manual cleaning, chemical cleaning with hydrochloric acid plus inhibitor to prevent acid attacking the metal without affecting removal of deposits is the best procedure.
4.      For oil contamination, alkali boil-out using tri-sodium phosphate solution is essential prior to acid cleaning. Through water flushing must be carried out after acid cleaning to avoid acid concentration in crevices and captive spaces.
5.      All internals that may interfere with the inspection have to be removed.
6.      Wherever adequate visual examination is not possible, surveyor may have to resort to drilling, ultrasonic, or hydraulic testing.
7.      All manhole doors and other doors must be opened for reasonable time previous to survey for ventilation.
8.      If another boiler is under steam arrangement of locking bar and other security devices must be in position preventing the admission of steam or hot water to the boiler under survey. The smoke trunking, exhaust gas shut-off etc., must be in position and in proper working condition.
9.      Plant’s staff or repairer’s staff should stand by the manhole in case of emergency and to take note for defects/ repairs required.
Before survey, the surveyor should acquaint himself with the boiler type in question (drawings carried on board) and during the survey it is advisable to follow a planned routine in order not to miss parts of the boiler or important items.