thermal power plant familarisation & its auxillaries
DESCRIPTION
PPT in Relation to Power Plant familarisation, Coal to Electricity Basics,Power Plant cycles, Concepts of Supercritical Technology Boiler, Concepts Of BTG Package as well as Balance of PlantTRANSCRIPT
POWER PLANT FAMILARISATION
(COAL BASED)
WHY TO OWN CAPTIVE POWER PLANT
Sl No
Description TG Set DG Set SEB
1Interruption of Power Supply
- NA - - NA - Possible
2Power Restriction / Demand Control
- NA - - NA - Possible
3Controlling of Voltage & Frequency
Possible Possible Not Possible
4 Initial Cost Very High High Less
5 Production CostRs. 2.75 /
UnitRs. 3.80 /
Unit
Demand : Rs. 150 / KVA
Energy : Rs. 7.15 / Unit
6 Pollution Problem Less Less Nil
7Banking / Selling of Excess Power
Possible Possible - NA -
8 Maintenance Cost Moderate Very High Less
FUEL
POWER PLANT
Non Conventional Fuel / Sources Conventional Fuel
WindSolar
OceanHusk
Baggas
DieselFurnace Oil
CoalLignite
Gas
Non-Conventional Fuel
Coal to Electricity ….. Basics
Coal
Chemical Energy
Super Heated Steam
Pollutants
Thermal Energy
Turbine Torque
Heat Loss In Condenser
Kinetic Energy
Electrical Energy
Alternating current in Stator
Mech. Energy Loss
ASHHeat
Loss
Elet. Energy Loss
POWER PLANT CYCLES
• SIMPLE RANKINE CYCLE.
• REHEAT CYCLE.
• REGENERATIVE CYCLE.
RANKINE CYCLE• The Carnot Cycle is theoretically most efficient, but it is
having practical difficulties.• For steam power plant, practical thermal cycle was
suggested by Rankine, called Ideal cycle or Rankine cycle.
3-3’ – BFP raises pressure from p2 to p1
3’-4 – Heating In feed heaters & eco
4 -1 – Heating In boiler
1-2 – Work done in Turbine from p1 to p2
1
23
3’
4
T
S
T1
T2
p1
p2
THERMAL EFFICIENCY OF RANKINE CYCLE Q1-Q2 W Useful work• η = ------- = --- = ----------------
Q1 Q Heat supplied
Rejected Heat • η = 1 - -------------------- Useful Heat
T1 - T2 T2• η Carnot = -------- = 1 - ---
T1 T1
• To achieve more efficiency T2 should be as low as
possible and T1 should be as high as possible
METHODS OF INCREASING RANKINE CYCLE EFFICIENCY
Raising supply temperature by super heating.
Increasing the inlet temperature will raise the heat supply to the
cycle more than the heat rejection.
Raising inlet pressure of steam : Increasing the pressure will mean increase in saturation
temperature at which steam evaporates thus increasing the average inlet temperature (T1)
Dropping the final pressure (or temperature) at which heat is
rejected.
Regenerative Heating : Heating the feed water pumped to Boiler
by bleeding steam from turbine.
Reheat Cycle : Reheating of steam in boiler after it has already
expanded in HP Turbine will avoid moisture formation in LT
Turbine. Also, more heat content of steam before IP Turbine,
will improve efficiency.
WHY SUPERCRITICAL PRESSURE
A Boiler operating at a pressure above critical point is called ‘SUPERCRITICAL BOILER’
A point where boiling water and dry saturated lines meet so that associated latent heat is zero, this point is called Critical Point and occurs at 225 kg/cm2 (abs) 374.15º C temperature.
CRITICAL CONDITION
Definition
“CRITICAL” is a thermodynamic expression describing the state of a substance beyond which there is no clear distinction between the liquid and gaseous phase.
• The critical pressure & temperature for water are • Pressure = 225.56 Kg / cm2• Temperature = 374.15° C
254 Kg/cm2
0
100
200
300
400
500
600
SUPER CRITICAL BOILER CYCLE WITH SH, RH & Regeneration
571°C 569°C
Steam flow :2111 T/HrSteam temp : 571 °CSteam Pres : 254 kg/cm2
RH pre : 47.3 Kg/cm2
RH Temp : 569°CFeed water Temp : 282°C
ENTROPY
TEMP
SUPERCRITICAL BOILER
• Supercritical pressure boiler has no drum and heat absorbing surface being, in effect, one continuous
tube, hence called ‘once through Supercritical pressure boilers.’
• The water in boiler is pressurized by Boiler Feed Pump, sensible heat is added in feed heaters, economizer and furnace tubes, until water attains saturation temperature and flashes instantaneously to dry saturated steam and super heating commences.
SUPERCRITICALTHERMAL CYCLE ADVANTAGES
• Improvements in plant efficiency by more than 2 %
• Decrease in Coal Consumption
• Reduction in Green House gases.
• Overall reduction in Auxiliary Power consumption.
• Reduction in requirement of Ash dyke Land & Consumptive water.
INCREASE IN PLANT EFFICIENCY by
SUPER CRITICAL PARAMETERS1.5
0.90.6
3.2
167 bar538/538’c
250 bar538/538
250 bar540/560’c
250 bar580/600’c
250bar566/566 ‘c
1
2
3
4
5
6
.
Efficiency Increase
COMPARISION OF THERMAL CYCLE EFFICIENCIES.
• OPEN CYCLE EFFICIENCY - 14.68 %
• WITH CONDENSER - 26.2 %
• WITH SUPER HEAT – 30.75 TO 34.15 %
• WITH REHEAT - 34.2 TO 36.6 %
• WITH SUPER CRITICAL PARAMETERS-
36.0 TO
39.15 %
• Efficiency of the cycle= Net W.D/Heat input
η = 1 - T2 T1 Where ,
T1 = Temp. of heat source
T2 = Temp. of heat sink
Steam Power Plant
Steam Theory
• Within the steam generator, fuel and air are force into the furnace by the burner.
• There, it burns to produce heat
• From there, the flue gases travel throughout the boiler.
• The water absorbs the heat, and eventually absorb enough to change into a gaseous state - steam.
• Boiler makers have developed various designs to squeeze the most energy out of fuel and to maximized its transfer to the water.
• To the right is the basic theoretical design of a modern boiler.
Furnace absorption
Platen SH
Divisional SHReheater
FSH
Economizer APH
Combustion Losses C & R losses
Hot Exhaust Gaslosses
MAJOR SECTIONS OF THERMAL POWER PLANT
• Coal Handling
• Boiler & its Auxiliaries
• Turbine & its Auxiliaries
• Cooling Tower & Condenser
• Water Treatment Plant & Water Handling
• Ash Handling System
CHS comprises of following systems:
Unloading System, Stacking, Screening & Crushing, Reclaiming, Bunker Feeding system.
GENERAL SYSTEM DESCRIPTION:
1.Unloading System
Coal Shall received at site through wagons and shall be unloaded by a. Wagon Tippler. b. Track Hoppers.
2. Stacking:
When boiler bunkers are full, coal shall be diverted to stockpile through reversible belt feeder.
The long travel Reversible Stacker cum Reclaimer shall be mounted on yard conveyers for stacking & reclaiming.
Normally, 2 nos of stock piles will be formed on each side of SCR. Total 4 nos stockpiles of trapezoidal cross section of height 10m, length 650m & width at base 49m. The storage capacity is for 15 days at 90 % PLF. Coal stored shall be (-) 100mm.
3. Screening & Crushing:Vibrating grizzly screens to separate (-) 25 mm coal before feeding the coal into crusher. (-) 100 mm coal size shall be fed to Ring Granular Type Crusher for crushing coal to (-) 25mm size. Crushed coal will be fed further into Boiler coal bunkers through belt conveyers.
4. Reclaiming:The coal from stock pile shall be reclaimed by bucket wheel reclaimer to feed onto reversible yard conveyer for conveying into crusher house.
5. Bunker Feeding system: Crushed coal from crushers shall be discharged onto belt
conveyers for feeding into junction towers. Coal from JT shall be fed into boiler coal bunkers with the help of travelling trippers.
Raw Coal
Belt Conveyor
Primary Screen
Crusher Less than 25MM
Secondary Screen
Belt Conveyor
Coal Bunker
More than 25mm Less than 25mm
BOILER
• WHAT IS BOILER
• TYPES OF BOILER
• CIRCULATION
WHAT IS BOILER
• A BOILER OR STEAM GENERATOR IS A CLOSED VESSEL IN WHICH STEAM IS GENERATED BY HEATING THE WATER BY COMBUSTION OF FUEL IN FURNACE.
• ANY CLOSED VESSEL EXCEEDING 22.75 LITRES IN CAPACITY WHICH IS USED EXPRESSLY FOR GENERATING STEAM UNDER PRESSURE AND INCLUDES ANY MOUNTING OR OTHER FITING ATTACHED TO SUCH A VESSEL WHICH IS WHOLLY OR PARTLY UNDER PRESSURE WHEN STEAM IS SHUT.
TYPES OF BOILER
1. MODE OF CIRCULATION OF WORKING FLUID2. TYPE OF FUEL3. MODE OF FIRING4. NATURE OF HEAT SOURCE5. WORKING PRESSURE6. SPECIFIC PURPOSE OF UTILISATION7. MANUFACTURERS TRADE NAME
CIRCULATION
• MOTION OF WORKING FLUIDS IN EVAPORATOR
TYPES CIRCULATION
1. NATURAL CIRCULATIONCIRCULATION BY MEANS OF DENSITY DIFFERENCE
2. FORCED CIRCULATIONCIRCULATION BY MEANS EXTERNAL FORCE LIKE PUMPING
Boiler Mixed Nozzle
Economizer
Chimney
ID fan
ESPAir Heater
FD Fan
PA Fan
Coal Bunker
Chain Feeder
Boiler Section – Flow DiagramSteam to Turbine
From HP Heater
Inle
t to
Boil
er
No. 1
HP Heater
BFBP
MD-BFP
CEP
GSC
No.7AB&8AB
LP Heater
No.5 LP Heater
DEAERATOR
CONDENSER
LPT LPT IPT HPT
No. 2
HP Heater
No. 3
HP Heater
BRCP
LTRH I/L Header
LTRH
ECO I/L Header
LTSH
ECO
No.6 LP Heater
HP BFWP
CRP
SEPARATOR
SEPARATOR
DRAIN TANK
ROOF TUBE
I/L Header
SH DIV Panel
FSHFRH
VERTICAL WATER WALL
SPIRAL WATER WALL
MSP
HRP
HP-BP
LP-BP
WW LOWER Header
GG
TD-BFP
A B
BA
A B C
Steam Turbine
• A steam turbine is a mechanical device that extracts thermal energy from pressurized steam, and converts it into useful mechanical work.
Steam Flows from Boiler to turbine
Bypass Turbine
HPT
IPT LPT A LPT B
CPU
GSC
Condensor (HP) Condenser
(LP)
2
HPH
- 1
HPH
- 2
HPH
-3
EXT From CRH
LPH -5LPH -6
LPH -7ALPH -7B
LPH -8ALPH -8B
3
Deaerator
BFBP
TDBFP
Boiler
CEP3x50%
2x50%
FCS
5 56 6
2x50%
From Reheater
Economiser
(MD BFP 1x35%)
(MD BFBP 1x35%)
78
78 8
778
1
Condenser
Extraction system of A Large Steam Turbine Reheat Steam
HP
Main Steam
Steam for Reheating
IP
LPLP
HPH HPH/TDBFP LPH
LPH
LPH
Condenser
Steam from last stage of LPT Exhausts on condenser tube
condensation of steam takes place
Water collected in hot well
Cooling Water System
HOT WATER
COLD WATER
Cold Water
Cooling Tower
CW Pump
Condenser
CCCW Pump
ACW Pump
Equipments
Heat Exchanger
Circulating water scheme
• A circulating water pump house • Intake channel• Trash rack• A chlorination plant• Traveling water screen• Connecting pipe line to condensed• Outlet channel• A cooling tower
Closed Loop system:
Condenser
River Flow
Steam from Turbine
Pump for make up
Hot mist
CW Pump
Cooling TowerHot water
Cold Water
CW scheme…
Reservoir/ River Canal Intake
Trash rack
TWS
CW pumps
Condenser
Hot Pond
CT pumps
Cooling tower
Condensate & Feed Water System
Low Pressure Heaters
D/A
Feed Storage Tank
High Pressure HeatersCEP-BCEP-A
BFPs
HOT WELL
Boiler
HOT WATER STEAMWARM WATER
A B C
Cascade Aerator
Gas Chlorination
Stilling Chamber
Raw Water
Flash Mixer Flocculator
Tube Settler
Clarified Water Storage Tank
To RO MB Plant
Poly-electrolyteFeCl3
Alum, Lime
Alum, Lime
Alum, Lime
PRE TREATMENT PLANT
Poly Dosing
Poly Dosing
Poly Dosing
Clarifier Soft Water Pumps
Clarified Water
Storage
Tank
Filter Feed
Pumps
CT Make Up Line
Multi Grade Filter
Ultra Filtratio
n
Micron Cartridge Filter
De- gassifier
RO Feed
Pumps
RO High Pressure Pumps
RO Membra
nes
RO Permit Tank
MB Feed
Pumps
Mixed Bed
DM Water Tanks
DM Water Distributi
on
Water Flow Diagram (WTP)
Water Flow Diagram(DM Water)
DM Water Tank
CondensateTank
De-Aerator Boiler Turbine
Water Cooled
Condenser
What is Ash
• Ash is Oxidized form of the mineral matters present in coal
• Typical ash composition:Sio2,Al2O
3,Fe
2O
3,CaO,MgO etc
• Coal with more Sio2 & Al
2O
3, Ash MP > 1400°C
• Coal with more Fe2O3, CaO & MgO Ash MP < 1100°C
General Description:Ash Handling System comprises of following sub
systems:
1. BOTTOM ASH HANDLING SYSTEM:A. Bottom Ash Hopper with accessoriesB. Bottom Ash Overflow Transfer SystemC. Bottom Ash area drain Transfer SystemD. Economizer Ash Disposal System
2. FLY ASH HANDLING SYSTEMA. Vacuum Conveying SystemB. Pressure Conveying System
3. SILO UNLOADING SYSTEM4. WATER SUPPLY SYSTEM5. ASH SLURRY DISPOSAL SYSTEM6. HANDLING FACILITIES (CRANES & HOISTS)7. ASH SLURRY SUMP ACCESSORIES8. ASH SLURRY TRANSPORT PIPING9. AIR CONDITIONING & VENTILATION SYSTEM
Bottom Ash Handling System
Ash Slurry Sump
Ash
Pon
d
Ash Slurry Pumps – 4 sets ASPH
Eco Hopper-6nos
Flushing Appratus-6nos
Overflow Tank
Overflow Pump Settling Tank
Sludge Pumps
Ash Water Sump
AW
PH
FAHP-4Nos, BAHP-3Nos, LPW-4Nos
Water
Sludge
Bottom Ash Hopper
Feed Gate
Jet PumpClinker Grinder
Fly Ash Handling System
Surge Hopper
ESP hoppers-
RCC Silo
Conveying Compressor-
IA Compressor
Vacuum Pump
Unloading spout for Railway Wagon
Unloading spout for Closed Tanker
Ash Conditioner for Open Truck
for future Expansion
APH Hopper-
Flushing Apparatus
Air Washer-
Seal Box-
3 cell Collector
Master D Pump
Slave D Pump
Wetting s
Ash Slurry Pump House
Collector Tak-
Silo Fluidizing Blower
From Fly Ash HP Water Pump
COOLING TOWER
CW PUMP
GENERATOR
GENERATOR
TRANSFORMER
COAL MILL
BUNKER
FD FAN PA FAN
ID FAN
STACK
APH
BOILER
DRUM
CEP
BFP
LPH
HPH
ESPCONDENSER
Koradi Super Critical Expansion Power Project site (3 x660 MW) - Sunil Hi-Tech Engineers Limited
Typical Modern Power Plant Turbine
CONDENSATE & FEED WATER SYSTEM
HOT WELL
HOT WELL
CONDENSER
GSCDRAIN
COOLERLPH-1 LPH-2
LPH-3EJECTOR
D/A
D/A FST
HPH-5HPH-6FRS
TO BOILER
LP DOZING
CEP-B
CEP-A
BFP-A,B,C
HP Turbine Rotor
LP Turbine Rotor