PREM BOILER EMERGENCIES.ppt

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    Boiler Emergencies of 500 MW

    R Prem Anand

    Manager

    NTPC LTD

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    Coal Mills Fire / PA Fan duct Fire

    Observations:

    Fire reported by Local Engineer

    Coal Mill outlet temperature going hi

    Coal Mill outlet temperature hi" annunciation on UCP / Alarm CRT

    Actions

    Inform Fire department

    Close Hot Air Gate of the coal mill having fire

    Unload and stop the coal mill having fire and close Cold Air Gate

    Ensure whether inert steam is applied

    Monitor coal mill outlet temperature

    In case of burner oil / gas pressure raising, take additional available guns orelevation in service

    Reduce the coal / fuel oil ratio pot for reducing the loading of other coal mills in

    case if they are on auto

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    FD Fan Stalling

    Observations

    Annunciation on UCB / Alarm CRT Combustion going bad

    Rise in MS & RH Steam temperature

    Difference in suction flow and current of both FD fans

    Actions

    Take blade pitch control of both the fans on manual and reduce slightly the loading of

    healthy fan seeing the current and suction flow - Boiler master on manual, Turbine follow

    mode

    In case the load is > 250 MW, adjust fuel firing equal to 250 MW Load

    Monitor boiler metal temperatures

    Operate blade pitch control of affected fan to minimum position and load the fan slowlyby watching current and suction flow

    When both FD fans are normal, put blade pitch control on Auto. Put Boiler master on

    Auto and select Boiler follow mode

    Increase generation as per requirement

    In case the affected fan blade pitch control link has given away, then follow procedure for

    one fan operation

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    Coal Mill Seal Air Differential Pressure Hi

    Observations

    Alarm on UCP / Alarm CRT

    Actions

    Inform OE / AOE (Boiler) to check Delta P from local indicator / transmitter

    If Delta P is on higher side, take standby filter in service

    Isolate choked filter

    Confirm with additional officer that no coal powder is coming out from journal bearing

    and if there is no improvement in Delta P, unload and take out corresponding coal mills

    In case of burner oil / gas pressure raising, take additional available guns or elevation in

    service

    Reduce the coal / fuel oil ratio pot for reducing the loading of other coal mills in case if

    they are on auto

    Stop seal air fans on that side and isolate

    Inform MMD

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    All LDO Oil Pumps Tripping

    Observations

    Alarm on UCP / Alarm CRT

    LDO Oil Pumps trip indication on UCP / CRT

    Fuel oil burner / header pressure zero

    Fuel oil elevations wipe out

    LDO oil CPRV goes close

    LDO oil trip valve goes close

    Runback active, load will drop to the capability coal mill (U5) in service

    Coal mill will get overloaded

    Boiler Trip in case of full oil firing leading to Main Turbine Trip

    Actions

    Inform AOE (Fuel) to rack out corresponding unit tripped LDO oil pumps breaker

    In case coal feeder are on auto, take coal feeders on manual and maintain coal flow within

    operating limits and stabilise load as per fuel firing

    In case of boiler trip - follow procedure for MFT and Main Turbine Trip

    Confirm the cause of LC oil pumps tripping

    Inform LD / EMD / MMD / IMD

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    RAPH Fire

    Observations

    For the RAPH on fire following annunciations will appear on Alarm CRT

    Flue Gas outlet temperature Hi-Hi

    RAPH Differential Pressure Hi-Hi Secondary Air Outlet Temperature Hi

    Furnace Draft Hi

    Combustion going bad

    Stack emission going bad

    Actions

    Monitor all the parameters

    Sound fire siren

    Inform Fire Department / LD / M(O)

    Prepare for One Fan Operation to isolate the RAPH on fire

    Drop Load to 250 MW by creating run-back by removing Coal Mills

    Close flue gas inlet & outlet damper of the referred RAPH

    Close air inlet & outlet damper of the referred RAPH

    Stop the RAPH on fire and its lube oil pumps

    Stop ID fans and the associated FD Fan

    Start RAPH wash pumps and extinguish RAPH fire

    Monitor parameters and stabilise the conditions at 250 MW

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    Loss of all Coal Mills with One LDO Oil elevation In Service

    Observations

    Annunciation on UCP / Alarm CRT

    Coal mills which are in service will trip on PA header pressure Lo

    Running PA Fans has gone in stalling mode

    Difference in PA Fan currents and Primary Air flow

    Runback active, Load will drop to the capability of fuel oil elevations in service

    Boiler master on manual, Turbine follow mode Boiler master goes negative

    Actions

    Take Fuel oil control on manual

    Take Fuel oil elevations in service Adjust Fuel oil CPRV bypass to bypass to have margin on CPRV

    Maintain Drum level, Dearator level and hotwell level

    Unload and load slowly PA Fan which has gone to stalling mode

    Normalise the conditions, Take controls on Auto

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    Excessive Drum Pressure Rising with HP / LP Bypass Available / Not

    Available

    Observations

    Alarm on UCP / LCN / Alarm CRT

    Drum pressure rising leading to boiler master deviation going positive

    Increase in throttle steam pressure

    Drop in Drum level, increase in BFP speed

    Main Turbine HP control valves throttling

    Reduction in fuel on auto

    Causes

    Main turbine HP control valves (throttling side)

    Superheater spray flow control valves (opening)

    Burner tilt (coming down) FD fans control vane (opening)

    Fuel control valves (opening)

    Coal feeder speed (increasing)

    Load throw off

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    Actions

    With HP / LP Bypass Available

    Increase load if margin is available. Inform LD

    If main turbine HP control valves are hunting, arrest the hunting by investigating the

    cause, else go for valve wide open operation

    Take main steam spray control valves on manual and reduce the superheater spray flow

    Take burner tilt on manual and raise it

    If FD fan/s control vane malfunctions, take control on manual and adjust secondary air

    flow according to load

    If fuel control valves malfunction, take control on manual and adjust fuel flow according

    to load

    Monitor fuel oil burner pressure, take fuel oil guns out of service if necessary

    Take coal feeders (which are in service) on manual and reduce coal flow accordingly

    Arrest the boiler master increasing

    At boiler master deviation of +10 bar, HP / LP bypass may come into service, start standbyCEP

    Note : During the disturbance

    Monitor condenser vacuum, drum level, deaerator level and hotwell level

    Monitor FD / ID / PA fan parameters

    Normalise the conditions when boiler master is normal

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    With HP / LP Bypass Not Available

    Increase load if margin is available. Inform LD

    If main turbine HP control valves are hunting, arrest the hunting by investigating the

    cause, else go for valve wide open operation Take main steam spray control valves on manual and reduce the superheater spray flow

    Take burner tilt on manual and raise it

    If FD fan/s control vane malfunctions, take control on manual and adjust secondary air

    flow according to load

    If fuel control valves malfunction, take control on manual and adjust fuel flow according

    to load

    Monitor fuel oil burner pressure, take fuel oil guns out of service if necessary

    Take coal feeders (which are in service) on manual and reduce coal flow accordingly

    Arrest the boiler master increasing

    If boiler master is still increasing, ERV (if available) will open on auto, else main steam /

    reheat steam lines safety valves may lift

    Note : During the disturbance

    Monitor condenser vacuum, drum level, deaerator level and hotwell level

    Monitor FD / ID / PA fan parameters

    Normalise the conditions when boiler master is normal

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    RAPH LUB Oil Pumps Tripping

    Observations

    Alarms on UCP / Alarm CRT

    Case1 - Only 1 Guide Bearing OR Support Bearing Lube Oil Pump TripsActions

    Inform Boiler OE / AOE and start standby Lube Oil Pump

    Check Lube Oil Tank level and Lube Oil Pump discharge pressure

    Monitor RAPH Bearing Temperature

    Case 2 - Both Guide Bearing Lube Oil Pumps not coming in service

    Actions

    Monitor Guide Bearing Temperature closely.

    Investigate the cause of Lube Oil Pumps not coming in service.

    In case Guide Bearing Temperature goes above 90 C,

    Inform LD and reduce Load to 250 MW for one Fan operation

    Follow procedure for one fan operation

    Case 3 - Both Support Bearing Lube Oil Pumps not coming in service

    Actions

    Monitor Support Bearing Temperature closely

    Check Tank level is OK

    Investigate the cause of Lube Oil Pumps not coming in service

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    One PA Fan Tripping

    Both PA Fans In Service

    Observations

    Annunciation on UCP / Alarm CRT

    Coal mills which are in service will trip on PA header pressure Lo

    Other PA Fan which is in service will get loaded to 100% and current > 210 amps

    Fuel oil flow will increase

    Runback active, Load will drop to the capability of fuel oil elevations in service Boiler master on manual, Turbine follow mode

    Boiler master goes negative

    Actions

    If Fuel oil is in service take control on manual other wise take fuel oil Adjust Fuel oil CPRV bypass to bypass to have margin on CPRV

    Maintain Drum level, Dearator level and hotwell level

    Unload the running PA Fan and maintain PA Fan current under limit

    Confirm that tripped PA Fan discharge damper has gone closed or get it closed manually

    Normalise the conditions, Take controls on Auto

    Note down the relay targets for the tripped PA Fan

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    Only One Fan In Service

    Observations

    Annunciation on UCP / Alarm CRT

    Coal mills which are in service will trip on PA header pressure Lo

    Actions

    If Fuel oi; is in service, take fuel oil control on manual

    Adjust Fuel oil CPRV bypass to bypass to have margin on CPRV

    Normalise the conditions, Take controls on Auto

    Note down the relay targets for the tripped PA Fan

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    Two PA Fan Tripping

    Observations

    Annunciation on UCP / Alarm CRT Coal mills which are in service will trip on PA header pressure Lo

    Unit tripping

    Boiler master goes negative

    Actions

    If Fuel oil is in service, take fuel oil control on manual

    Adjust Fuel oil CPRV bypass to bypass to have margin on CPRV

    Maintain Drum level, Dearator level and hotwell level

    Normalise the conditions, Take controls on Auto

    Confirm the relay targets for the tripped PA Fans

    If Boiler trips follow MFT procedure.

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    One FD Fan Tripping

    Observations

    FD Fan trip annunciation / indication on UCP / LCN / Alarm CRT

    Load runback to 300 MW (if load was more than 300 MW)

    Corresponding ID Fans will trip

    Actions

    In case of runback, follow procedure for runback active

    Ensure that sufficient airflow is maintained for proper combustion (if required take running

    FD fan blade pitch control may be taken on manual)

    Coal mills may trip due to PA header pressure Lo, on loss of PA Fan, take fuel oil / gas

    elevation(s) in service as per requirement. (Fuel oil / gas elevations adjacent to the tripped

    coal mills can not be taken in service for 180 seconds after tripping of coal mills)Maintain drum level, deaerator level and hotwell level

    Stabilise the conditions

    Ensure that outlet damper of FD fan that has tripped goes close

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    FURNACE PRESSURE HIGH

    One I.D. Fan tripped or Mal-operation

    of control vanes of I.D./F.D./P.A. Fans or closing of

    damper

    Unstable furnace flame conditions.

    Furnace water seal broken, E.P. or flue gas path

    manhole opened.

    Water wall tube rupture/leakage.

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    FURNACE PRESSURE LOW

    I.D. Fan auto control Failure.

    I.D. Fan vane control mechanism Failure causing

    vanes to open wide.

    Sudden decrease in air input or tripping of one

    F. D. fan.

    Sudden tripping of one or more mills or choking

    of mill/raw coal Feeder pipe.

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    ID FAN TRIP

    Electrical protection trip.

    Emergency Push Button pressed.

    Stop command from UCB.

    Post trip purge furnace pressure high/low.

    Fan/Motor bearing temperature high-high. (>1000

    C)

    Lube oil pressure low-low. (850

    C)

    Hydraulic coupling oil temperature high-high.

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    FD FAN TRIPPED

    Running FD fan trips in case of the following:

    Electrical protection trip.

    Emergency PB pressed.

    Stop command from UCB.

    No ID fan running or one ID fan and one FD fan already in

    service.

    Post trip purge furnace pressure high/low.

    Fan/Motor bearing temperature high-high.(>1000 C)

    Dampers fail to open in 180 sec after fan starting.

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    PA FANS Logics :1. Hot PA header pr. Low -560 mm WCL

    2. Hot PA header pr. Lowlow

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    PA FAN TRIPPED

    If a running PA fan trips, then : If 5 or more than 5 mills are in service ,the tripping will

    be as follows :

    H mill trips immediately

    G mill trips 2 sec. delay

    F mill trips 4 sec. delay

    E mill trips 6 sec. delay

    When 4 mills are ON then, PA Fan trip signal causing

    mills trip will not be effective.

    (When one PA or one FD fan trips ,the sequence is same

    as above)

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    PA fan tripping

    Effects :

    - Top two mill will trip on FSSS interlock

    - Unit load may come down to approx. 300MW

    - PA header pressure will come down

    - Other running PA fan may get overloaded

    Action:

    -Other PA fan loading to be reduced to avoid its

    overloading (if it is in auto)- Reduction of sec. air flow

    (excess sec. air will disturb the flame)

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    FD or PA fan stalling

    Effect :

    Stalled fans current will come down

    Stalled fans discharge will reduce

    Vibration of fan will increase

    Abnormal sound in local Other fan may get overloaded.

    sec air flow or pa flow will reduce.

    Action :

    Reduce other fans loading ( if it is in auto take inmanual).

    Match both fans loading.

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    AIR PRE-HEATER

    Air pre heater bearing temperature very high.

    Air pre-heater electric motor tripped.

    APH electric drive tripped and air motor fails

    to start.

    Air pre-heater on fire.

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    DRUM LEVEL LOWMal-operation of Feed Auto Control or Feed Regulator or

    scoop auto.Tripping of one of working feed pump (standby pump

    does not start)

    Sudden increase of load.

    Sudden increase in firing rate

    Starting of mills having sufficient coal left before previous

    stopping.

    Tube rupture/puncture of low point drain valves orEmergency drum drain Valve

    Inadvertant opening of low point drain valves or

    Emergency Blowdown (EBD) valve/CBD valve.

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    HIGH DRUM LEVEL

    Mal-operation of feed water control.

    Sudden decrease in firing rate e.g. tripping of

    the running mills.

    B.F.P. Scoop tube position suddenly increased.

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    FLAME FAILURE AT AN ELEVATION

    Closing of trip valves on H.F.O. Oil/ Ignitor (Causing loss of

    ignition support energy) Where HFO is being used as

    support fuel or when only oil is being used

    Sudden decrease of mill feeder speeds to minimum.

    Too low or too high wind box pressure causing unstable

    combustion. Water wall tube failure

    Malfunction of flame scanners due to supply failure or

    scanner air failure,

    Slag or soot on scanner lenses etc.

    Burner tilt mechanism negative extreme due to air failure

    to power cylinders.

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    ONE FEEDER TRIPS

    Effect :

    No coal flow alarm comes.

    Mill trips

    Support energy is removed within 3 minutes

    of feeder starting.

    Load gets affected

    ONE MILL TRIPS

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    ONE MILL TRIPS

    Auto stop command is present.

    Stop PB operated from FSSS console in manual mode. Primary air trip command is present.

    Boiler trip.

    Pulveriser discharge valve not open.

    Ignition permit required and ignition permit lost.

    Lub oil pressure low trip.

    EPB pressed.

    Seal air header / pulveriser under bowl DP is < 5 WCL.

    Elevation power not available for more than 2 sec.

    Pulveriser can be started after 2 sec of trip.

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    WATER WALL TUBE LEAKAGE

    Starved water walls due to very low drumlevel.

    Sustained flame impingement on water walltubes.

    Blocked tube, scaling of tube, resulting inoverheating of tube metal, pitting, corrosion oftubes.

    Soot blower steam impingement (wet steamimpingement or direct impingement of steam).

    Circulation affected due to opening of lowpoint drains.

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    SGWC or CC PUMP trip

    Running SGWC pump trips in case of the followingconditions :

    Discharge valve - 1 not fully open

    Discharge valve - 2 not fully open

    Motor cavity temperature high - 60oCEffect :

    Pump DP will come down

    Drum level may go high

    Action :

    Reduce BLI below 60% (MCR 1720 t/hr)

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    ECONOMISER /SUPFRHEATER/ REHEATER

    TUBE FAILURE

    Sustained high metal temperatures due to water wallSlagging or forcing boiler at the time of hot restart.

    Erosion on tubes due to high excess air, high ashcontent in coal dislocated tubes, soot blowing.

    Blocked tubes causing overheating.Salt deposition due to high water level in drum, poor

    quality of water.

    Inadequate flow due to open superheater, reheater

    drain.