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Master Fuel Trip Logic
Circulating Fluidized Bed (CFB) Boiler
Contents
• Process Followed
• Segregation of Control Systems in DCS
• Major Boiler Hazards, Causes & Protections
• Master Fuel Trip (MFT)
• How is MFT generated?
• What are the post MFT actions?
• Logics are referenced from EPTL logic
• In presentation, logics are presented in simplified manner
Process Followed
Includes
• Hub Power Station
Boiler Protection Logic
Scope
Development
Bench Marking Internal Review
Includes
• E&I Team Internal Review
• Cross Functional Review
Includes
• Design Review
• NFPA-85 ( Boiler and
Combustion Hazards Code)
• EPTL Logic diagram
Literature Review
Segregation of Control Systems in DCS
• Used for indication of values to the operator
• Example: Individual fluidizing air blowers outlet pressure
DAS
(Data Acquisition System)
• Used for the controlling of process.
• Example: Fluidizing air blowers pressure control.
MCS
(Modulating Control System)
• Used for sequential control & interlocks (on/off operation)
• Example: Fluidizing air blower cut-in logic.
SCS
(Sequential Control System)
• Used for sequential control & interlocks of burners and coal feeders. It can be
considered as a special purpose SCS.
• Example: Tripping of individual burner on its loss of flame.
BMS
(Burner Management System)
• Used for boiler protection.
• Example: Master Fuel Trip (MFT) on furnace pressure very high.
FSSS
(Furnace Safety &Supervision
System)
Boiler Hazards – Boiler Explosion
Un-burnt Fuel
• Improper combustion
will lead to unburnt
fuel
• Accumulated fuel will
create vapor / gas
mixture
• On Light-up this
mixture can cause
explosion
Trips:
• Air flow < 25%
• Loss of both PA fans (Only on coal fuel)
• Furnace temp LL (Only on coal fuel)
• Loss of all flame (Only on oil fuel)
Purge Requirement before start-up:
• If Furnace Temp < Adequate
Boiler Hazards – Boiler Explosion
Furnace Over
Pressure
• Balanced draft boiler
(SA and ID fans)
• Draft Imbalance will
cause disturbance
furnace pressure
• Over pressurized
furnace can explode
Trips:
• Loss of both ID Fans
• Furnace pressure HH (152 mmH2O)
• Less than 02 Fluidizing Air blowers running
• After MFT, if furnace press HHH (254mmH2O), then cut-
out both PA and SA Fans
Load Rejection:
• If single ID Fan trips, then cut-out corresponding SA
fan.
Boiler Hazards – Boiler Implosion
Furnace Under
Pressurization
• Balanced draft boiler
(SA and ID fans)
• Draft Imbalance will
cause disturbance
furnace pressure
• Excessive Negative
Pressure in furnace can
cause implosion
Trips:
• Trip on loss of both SA Fans
• Trip on furnace pressure LL (220mmH2O)
• After MFT if furnace pressure LLL (229mmH2O), then trip both
ID fans
Load Rejection:
• If single SA Fan trips, corresponding ID fan trips as well
Boiler Hazards – Boiler Tube Failure
Over Temperature
• Different causes like
steam / water starvation
in water wall tubes can
excessive temperature
• It can cause boiler tubes
to fail
Trips:
• Drum Water LL (-254mm)
Boiler Trip Conditions
S.No Boiler Trip
1 Both SA Fans Stopped
2 Both ID Fans Stopped
3 Turbine Trip
4 MFT Push Button
5 Total Air Flow < 25% (5 sec)
6 Furnace Pressure HH (152mm H2O)
7 Furnace Pressure LL (-220 mm H2O)
8 Drum Level HH (+254 mm) (5 seconds)
9 Drum Level LL (-254 mm) (5 seconds)
10 Less than 02 Fluidized Air Blower Running
11 Loss of Fuel Trip
12 Furnace Temp <620 C AND Both PAF Stopped
13 Both PAF Stopped (On Coal Fuel Only)
14 Primary Air Flow (On Coal Fuel Only)
15 Furnace Temp < Adequate (On Coal Fuel Only)
Signals for Boiler Load Rejection
S.No Boiler Load Rejection
1 Fuel Flow < Demand
2 Air Flow < Demand
3 Feed Water Flow < Demand
4 Primary Air Pressure < Demand
5 Fluidizing Air Pressure < Demand
6 Furnace Temperature < Demand
7 Drum Pressure < Demand
8 First Stage Pressure < Demand
9 Turbine Inlet Pressure < Demand
10 Either ID Fan Trip
11 Either SA Fan Trip
12 Either PA Fan Trip
13 Either Turbine Driven FWP Trip
MFT ( Main Fuel Trip)
BOTH SAFs STOPPED
BOTH IDFs STOPPED
TURBINE TRIP
MFT PUSH BUTTON
TOTAL AIR FLOW < 25% (5 sec)
FURNACE PRESSURE HH
(152 mm H2O)
FURNACE PRESSURE LL
(-220 mmH2O)
DRUM LEVEL LL (5 sec)
DRUM LEVEL HH (5 sec)
LOSS OF FUEL TRIP (LOFT)
<2 FLUID AIR BLOWERS ON
CONDITION # 1
CONDITION # 2
CONDITION # 3
OR
RESET
PURGE COMPLETED
MFT
PULSE:
( 5 sec )
Condition #1
FURNACE TEMPERATURE <
ADEQUATE (620°C)
BOTH PAF STOPPED
ANY COAL FEEDER ON
ANY COAL CONVEYOR (A/K)
ON
NO START-UP BURNER OIL
VALVE OPEN
AND
AND
OR CONDITION # 1
Condition #2
AND
ANY COAL FEEDER ON
ANY COAL CONVEYOR (A/K) ON
NO START-UP BURNER OIL
VALVE OPEN
PRIMARY AIR FLOW LOW
CONDITION # 2
Condition #3
AND
ANY COAL FEEDER ON
ANY COAL CONVEYOR (A or K)
ON
NO START-UP BURNER OIL
VALVE OPEN
FURNACE TEMPERATURE <
ADEQ FOR SOLID FUEL
CONDITION # 3
Furnace Purge
FSSS DPU POWER NO ALARM
AND
ALL SU BURNERS NO FLAME
ALL SU BNRS OIL TRIP VLVS CLSD
ALL COAL FEEDERS OFF
ALL COAL FEEDER TRIP VLV CLSD
EITHER PA FAN ON
ALL LS ROTARY VALVE OFF
PA FLOW >30%
NO MFT CONDITION STANDING
ALL COAL CONVEYOR (A&K) OFF
ALL SU BNRS AIR DMPERS OPEN
AND
NOT RESET
DELAY TIMER :
0 min 5 min
FURN.
TEMP.>ADEQ FOR
SOLID FUEL
NOT
PURGE
COMPLETE
PURGE
INPROGRESS
PURGE
BREAK
PURGE START COMMAND
AND
Post MFT Actions
All coal feeder will STOP
All individual burner oil valve will CLOSE
Oil supply main oil valve will CLOSE
Boiler air flow control to MANUAL
Boiler soot blower will STOP
Limestone feeders will STOP
Turbine BFPs inlet steam valves to CLOSE, and motor-BFP to START
Turbine Trip will INITIATE
Special Situations for Boiler Fans (1/2)
FURNACE PRESSURE LLL
(-229 mmH2O)
MFT DELAY TIMER
( 20 sec )
AND
FURNACE PRESSURE HHH
(254 mmH2O)
MFT
ID Fans Trip
AND
BOTH SA FANs TRIP
SA Fans Trip
PA Fans Trip
FABs Trip
SA Fans Trip
PA Fans Trip
FABs Trip
ID Fans Trip
ID Fans Trip
PA Fans Trip
FABs Trip
Special Situations for Boiler Fans (2/2)
BOTH ID FANs TRIP
LESS THAN 02 FABs RUNNING
DRUM LEVEL LL (-254 mm)
PA Fans Trip
PA Fans Trip
SA Fans Trip
PA Fans Trip
FABs Trip
Way Forward
Following protections need further review:
1. MFT on Furnace Temperature LL (820 °C on coal fuel)
• NFPA 85, sets this limit to 649 °C
2. MFT on Fluidizing Air Blower < 02 running
• To be reviewed for low load scenario.
3. MFT on Turbine Trip
• Considering the HP/LP bypass provision, MFT on turbine trip needs to be reviewed
4. MFT on Drum Level HH
• Utility of boiler trip on Drum Level HH to be reviewed
5. MFT on Furnace Temp HH
• Introduction of Furnace Temp HH trip to be evaluated.
THANK YOU
BACK UP SLIDES
LOFT (Loss of Fuel Trip)
ANY COAL FEEDER ON
ANY COAL CONVEYOR (A or K)
ON
ANY START-UP BURNER OIL
VALVE OPEN
ALL COAL FEEDER OFF
FUEL OIL HEADER SHUTOFF
VALVE OPEN
MFT > 5 sec
ANY INDUCT BURNER OIL
VALVE OPEN
ALL COAL CONVEYOR (A, K)
OFF
OR
OR
NOT
OR
NOT
S
AND
LOFT
R
Special Conditions Matrix
Selected Inputs Outputs
MFT(20 sec) and Furnace Press LLL
ID Fan Trip
SA Fan Trip (corresponding)
Drum Level LL
PA Fan Trips
MFT and Furnace Press HHH
More than 02 FABs stopped
Both ID Fan Trips
ID Fan trip (corresponding)
SA Fan Trips
MFT and Furnace Press HHH
Both ID Fans Trip
Both ID Fans Trip FAB Trips
Furnace Temperature (1/2)
FURNACE UPPER FRONT TEMP 8
FURNACE LOWER FRONT TEMP 8
FURNACE UPPER FRONT TEMP 7
AVERAGE
FURNACE UPPER FRONT TEMP 6
FURNACE LOWER FRONT TEMP 6
FURNACE LOWER FRONT TEMP 5
AVERAGE
FURNACE LOWER REAR TEMP 1
FURNACE UPPER REAR TEMP 1
FURNACE LOWER REAR TEMP 2
AVERAGE
FURNACE UPPER REAR TEMP 2
FURNACE LOWER REAR TEMP3
FURNACE UPPER REAR TEMP 3
AVERAGE
FURNACE LOWER REAR TEMP 4
FURNACE UPPER REAR TEMP 4
AVERAGE
H/L
(510°C)
H
L
H
AVERAGE
H/L
(650°C)
H
L
H
L
H/L
(***°C)
H
L
SOLID FUEL
PERMIT
SU BURNER CAN
BE TURNED
DOWN
FURNACE
TEMP>ADEQ FOR
SOLID FUEL
Furnace Temperature (2/2)
FURNACE UPPER FRONT TEMP 8
FURNACE LOWER FRONT TEMP 8
FURNACE UPPER FRONT TEMP 7
AVERAGE
FURNACE UPPER FRONT TEMP 6
FURNACE LOWER FRONT TEMP 6
FURNACE LOWER FRONT TEMP 5
AVERAGE
H/L
(620°C)
H
L
H
H
L
H/L
(620°C)
H
L
AND
FURNACE
TEMP>ADEQ
OFT (Oil Fuel Trip)
MANUAL OFT PUSH BUTTON
MFT
ALL OIL BURNERS VALVE
CLOSED
FUEL OIL HEADER SHUTOFF
VALVE CLOSED
ANY BURNER VALVE CLOSE
FAILURE
NO MFT
ALL OIL BURNERS VALVE
CLOSED
AND
OR
RESET
OFT
Air Flow Measurement
Total Air Flow
Primary Air Flow
Hot PA – Right (Average)
x03
Hot PA – Left (Average)
x03
Cold PA
(Sum of Coal Feeder PA)
x10
Fluidizing Air Blower Flow
Cyclone A
(Sum of FAB entering into
seal pot)
x02
Cyclone B
(Sum of FAB entering into
seal pot)
x02
Cyclone C
(Sum of FAB entering into
seal pot)
x02
Secondary Air Flow
SA Left
(Sum of SA entering into
furnace Left side)
x10
SA Right
(Sum of SA entering into
furnace Left side)
x10
Burner SA
(Sum of B,C,D,E)
x04

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FSSS_Logic Presentation - Modified_v11.pptx

  • 1. Master Fuel Trip Logic Circulating Fluidized Bed (CFB) Boiler
  • 2. Contents • Process Followed • Segregation of Control Systems in DCS • Major Boiler Hazards, Causes & Protections • Master Fuel Trip (MFT) • How is MFT generated? • What are the post MFT actions? • Logics are referenced from EPTL logic • In presentation, logics are presented in simplified manner
  • 3. Process Followed Includes • Hub Power Station Boiler Protection Logic Scope Development Bench Marking Internal Review Includes • E&I Team Internal Review • Cross Functional Review Includes • Design Review • NFPA-85 ( Boiler and Combustion Hazards Code) • EPTL Logic diagram Literature Review
  • 4. Segregation of Control Systems in DCS • Used for indication of values to the operator • Example: Individual fluidizing air blowers outlet pressure DAS (Data Acquisition System) • Used for the controlling of process. • Example: Fluidizing air blowers pressure control. MCS (Modulating Control System) • Used for sequential control & interlocks (on/off operation) • Example: Fluidizing air blower cut-in logic. SCS (Sequential Control System) • Used for sequential control & interlocks of burners and coal feeders. It can be considered as a special purpose SCS. • Example: Tripping of individual burner on its loss of flame. BMS (Burner Management System) • Used for boiler protection. • Example: Master Fuel Trip (MFT) on furnace pressure very high. FSSS (Furnace Safety &Supervision System)
  • 5. Boiler Hazards – Boiler Explosion Un-burnt Fuel • Improper combustion will lead to unburnt fuel • Accumulated fuel will create vapor / gas mixture • On Light-up this mixture can cause explosion Trips: • Air flow < 25% • Loss of both PA fans (Only on coal fuel) • Furnace temp LL (Only on coal fuel) • Loss of all flame (Only on oil fuel) Purge Requirement before start-up: • If Furnace Temp < Adequate
  • 6. Boiler Hazards – Boiler Explosion Furnace Over Pressure • Balanced draft boiler (SA and ID fans) • Draft Imbalance will cause disturbance furnace pressure • Over pressurized furnace can explode Trips: • Loss of both ID Fans • Furnace pressure HH (152 mmH2O) • Less than 02 Fluidizing Air blowers running • After MFT, if furnace press HHH (254mmH2O), then cut- out both PA and SA Fans Load Rejection: • If single ID Fan trips, then cut-out corresponding SA fan.
  • 7. Boiler Hazards – Boiler Implosion Furnace Under Pressurization • Balanced draft boiler (SA and ID fans) • Draft Imbalance will cause disturbance furnace pressure • Excessive Negative Pressure in furnace can cause implosion Trips: • Trip on loss of both SA Fans • Trip on furnace pressure LL (220mmH2O) • After MFT if furnace pressure LLL (229mmH2O), then trip both ID fans Load Rejection: • If single SA Fan trips, corresponding ID fan trips as well
  • 8. Boiler Hazards – Boiler Tube Failure Over Temperature • Different causes like steam / water starvation in water wall tubes can excessive temperature • It can cause boiler tubes to fail Trips: • Drum Water LL (-254mm)
  • 9. Boiler Trip Conditions S.No Boiler Trip 1 Both SA Fans Stopped 2 Both ID Fans Stopped 3 Turbine Trip 4 MFT Push Button 5 Total Air Flow < 25% (5 sec) 6 Furnace Pressure HH (152mm H2O) 7 Furnace Pressure LL (-220 mm H2O) 8 Drum Level HH (+254 mm) (5 seconds) 9 Drum Level LL (-254 mm) (5 seconds) 10 Less than 02 Fluidized Air Blower Running 11 Loss of Fuel Trip 12 Furnace Temp <620 C AND Both PAF Stopped 13 Both PAF Stopped (On Coal Fuel Only) 14 Primary Air Flow (On Coal Fuel Only) 15 Furnace Temp < Adequate (On Coal Fuel Only)
  • 10. Signals for Boiler Load Rejection S.No Boiler Load Rejection 1 Fuel Flow < Demand 2 Air Flow < Demand 3 Feed Water Flow < Demand 4 Primary Air Pressure < Demand 5 Fluidizing Air Pressure < Demand 6 Furnace Temperature < Demand 7 Drum Pressure < Demand 8 First Stage Pressure < Demand 9 Turbine Inlet Pressure < Demand 10 Either ID Fan Trip 11 Either SA Fan Trip 12 Either PA Fan Trip 13 Either Turbine Driven FWP Trip
  • 11. MFT ( Main Fuel Trip) BOTH SAFs STOPPED BOTH IDFs STOPPED TURBINE TRIP MFT PUSH BUTTON TOTAL AIR FLOW < 25% (5 sec) FURNACE PRESSURE HH (152 mm H2O) FURNACE PRESSURE LL (-220 mmH2O) DRUM LEVEL LL (5 sec) DRUM LEVEL HH (5 sec) LOSS OF FUEL TRIP (LOFT) <2 FLUID AIR BLOWERS ON CONDITION # 1 CONDITION # 2 CONDITION # 3 OR RESET PURGE COMPLETED MFT PULSE: ( 5 sec )
  • 12. Condition #1 FURNACE TEMPERATURE < ADEQUATE (620°C) BOTH PAF STOPPED ANY COAL FEEDER ON ANY COAL CONVEYOR (A/K) ON NO START-UP BURNER OIL VALVE OPEN AND AND OR CONDITION # 1
  • 13. Condition #2 AND ANY COAL FEEDER ON ANY COAL CONVEYOR (A/K) ON NO START-UP BURNER OIL VALVE OPEN PRIMARY AIR FLOW LOW CONDITION # 2
  • 14. Condition #3 AND ANY COAL FEEDER ON ANY COAL CONVEYOR (A or K) ON NO START-UP BURNER OIL VALVE OPEN FURNACE TEMPERATURE < ADEQ FOR SOLID FUEL CONDITION # 3
  • 15. Furnace Purge FSSS DPU POWER NO ALARM AND ALL SU BURNERS NO FLAME ALL SU BNRS OIL TRIP VLVS CLSD ALL COAL FEEDERS OFF ALL COAL FEEDER TRIP VLV CLSD EITHER PA FAN ON ALL LS ROTARY VALVE OFF PA FLOW >30% NO MFT CONDITION STANDING ALL COAL CONVEYOR (A&K) OFF ALL SU BNRS AIR DMPERS OPEN AND NOT RESET DELAY TIMER : 0 min 5 min FURN. TEMP.>ADEQ FOR SOLID FUEL NOT PURGE COMPLETE PURGE INPROGRESS PURGE BREAK PURGE START COMMAND AND
  • 16. Post MFT Actions All coal feeder will STOP All individual burner oil valve will CLOSE Oil supply main oil valve will CLOSE Boiler air flow control to MANUAL Boiler soot blower will STOP Limestone feeders will STOP Turbine BFPs inlet steam valves to CLOSE, and motor-BFP to START Turbine Trip will INITIATE
  • 17. Special Situations for Boiler Fans (1/2) FURNACE PRESSURE LLL (-229 mmH2O) MFT DELAY TIMER ( 20 sec ) AND FURNACE PRESSURE HHH (254 mmH2O) MFT ID Fans Trip AND BOTH SA FANs TRIP SA Fans Trip PA Fans Trip FABs Trip SA Fans Trip PA Fans Trip FABs Trip ID Fans Trip ID Fans Trip PA Fans Trip FABs Trip
  • 18. Special Situations for Boiler Fans (2/2) BOTH ID FANs TRIP LESS THAN 02 FABs RUNNING DRUM LEVEL LL (-254 mm) PA Fans Trip PA Fans Trip SA Fans Trip PA Fans Trip FABs Trip
  • 19. Way Forward Following protections need further review: 1. MFT on Furnace Temperature LL (820 °C on coal fuel) • NFPA 85, sets this limit to 649 °C 2. MFT on Fluidizing Air Blower < 02 running • To be reviewed for low load scenario. 3. MFT on Turbine Trip • Considering the HP/LP bypass provision, MFT on turbine trip needs to be reviewed 4. MFT on Drum Level HH • Utility of boiler trip on Drum Level HH to be reviewed 5. MFT on Furnace Temp HH • Introduction of Furnace Temp HH trip to be evaluated.
  • 22. LOFT (Loss of Fuel Trip) ANY COAL FEEDER ON ANY COAL CONVEYOR (A or K) ON ANY START-UP BURNER OIL VALVE OPEN ALL COAL FEEDER OFF FUEL OIL HEADER SHUTOFF VALVE OPEN MFT > 5 sec ANY INDUCT BURNER OIL VALVE OPEN ALL COAL CONVEYOR (A, K) OFF OR OR NOT OR NOT S AND LOFT R
  • 23. Special Conditions Matrix Selected Inputs Outputs MFT(20 sec) and Furnace Press LLL ID Fan Trip SA Fan Trip (corresponding) Drum Level LL PA Fan Trips MFT and Furnace Press HHH More than 02 FABs stopped Both ID Fan Trips ID Fan trip (corresponding) SA Fan Trips MFT and Furnace Press HHH Both ID Fans Trip Both ID Fans Trip FAB Trips
  • 24. Furnace Temperature (1/2) FURNACE UPPER FRONT TEMP 8 FURNACE LOWER FRONT TEMP 8 FURNACE UPPER FRONT TEMP 7 AVERAGE FURNACE UPPER FRONT TEMP 6 FURNACE LOWER FRONT TEMP 6 FURNACE LOWER FRONT TEMP 5 AVERAGE FURNACE LOWER REAR TEMP 1 FURNACE UPPER REAR TEMP 1 FURNACE LOWER REAR TEMP 2 AVERAGE FURNACE UPPER REAR TEMP 2 FURNACE LOWER REAR TEMP3 FURNACE UPPER REAR TEMP 3 AVERAGE FURNACE LOWER REAR TEMP 4 FURNACE UPPER REAR TEMP 4 AVERAGE H/L (510°C) H L H AVERAGE H/L (650°C) H L H L H/L (***°C) H L SOLID FUEL PERMIT SU BURNER CAN BE TURNED DOWN FURNACE TEMP>ADEQ FOR SOLID FUEL
  • 25. Furnace Temperature (2/2) FURNACE UPPER FRONT TEMP 8 FURNACE LOWER FRONT TEMP 8 FURNACE UPPER FRONT TEMP 7 AVERAGE FURNACE UPPER FRONT TEMP 6 FURNACE LOWER FRONT TEMP 6 FURNACE LOWER FRONT TEMP 5 AVERAGE H/L (620°C) H L H H L H/L (620°C) H L AND FURNACE TEMP>ADEQ
  • 26. OFT (Oil Fuel Trip) MANUAL OFT PUSH BUTTON MFT ALL OIL BURNERS VALVE CLOSED FUEL OIL HEADER SHUTOFF VALVE CLOSED ANY BURNER VALVE CLOSE FAILURE NO MFT ALL OIL BURNERS VALVE CLOSED AND OR RESET OFT
  • 27. Air Flow Measurement Total Air Flow Primary Air Flow Hot PA – Right (Average) x03 Hot PA – Left (Average) x03 Cold PA (Sum of Coal Feeder PA) x10 Fluidizing Air Blower Flow Cyclone A (Sum of FAB entering into seal pot) x02 Cyclone B (Sum of FAB entering into seal pot) x02 Cyclone C (Sum of FAB entering into seal pot) x02 Secondary Air Flow SA Left (Sum of SA entering into furnace Left side) x10 SA Right (Sum of SA entering into furnace Left side) x10 Burner SA (Sum of B,C,D,E) x04

Editor's Notes

  1. How is BMS diff frm SCS? Remember all all setpoints PA Flow: 620 t/h SA Flow : 660 t/h Comb Air Flow: 1380 t/h -- Fluidized Air Flow 100 t/h Fluidized Air Blower Pressure: Manually entered set-point
  2. PA Flow: 620 t/h SA Flow : 660 t/h Comb Air Flow: 1380 t/h -- Fluidized Air Flow 100 t/h Furnace Temp: 510 deg C (fuel oil permint) if burners > 4 ( NFPA 85: 482 deg C for solid fuel) or 820 deg C regardless of sub burners 650 Oil SU burners can be shutdown 820 deg C; if only on coal trip; (NFPA 85: must be >649 deg C for coal; but also testing; or as safe point >760) , PA Fan LL
  3. Furnace Press HHH 254 mm H2O Furnace Press HH 152 mm H2O Furnace Press Normal= -12kPa --0.12 bar Furnace Press LL -220 mm H20 Furnace Press LLL -229 mm H20
  4. Drum Level LL = -254 mm
  5. Bed temp High not included Drum Level LL -254mm H2O Drum Level HH 254mm H2O
  6. Furnace Temp 510
  7. Normal Furnace temperature is 850+/-25 °C Our 820 Normally >760 > 649 for coal