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PRESENTED BY
SAMRIDDHA SHIL
MECHANICAL ENGINEER
1
GARGI MEMORIAL INSTITUTE OF
TECHNOLOGY
2
What is Supercritical Pressure ?
Critical point in water vapour cycle is a
thermodynamic state where there is no clear
distinction between liquid and gaseous state
of water.
Water reaches to this state at a critical
pressure above 22.1 MPa and 374 o
C.
 1 - 2 > CEP work
 2 – 2s > Regeneration
 2s - 3 > Boiler
Superheating
 3 – 4 > HPT expansion
 4 – 5 > Reheating
 5 – 6 > IPT & LPT
Expansion
 6 – 1 > Condenser Heat
rejection
3
4
AbsoluteAbsolute
PressurePressure
(Bar)(Bar)
SaturationSaturation
TemperatureTemperature
((oo
C)C)
Latent HeatLatent Heat
(K J/Kg.)(K J/Kg.)
5050
150150
200200
221221
264264
342342
366366
374374
16401640
10041004
592592
00
VARIATION OF LATENT HEAT
WITH PRESSURE
5
Supercritical Boiler Water Wall
Rifle Tube And Smooth Tube
From CRH Line
From FRS Line
Boiler
Recirculation Pump
Economizer
Phase 1
Economizer
Phase 2
LTRH
LTSH
4430
C
FRH
Platen
Heater
Mixer Header
FSH
To HP
Turbine To IP
Turbine
Separator
Bottom Ring
Header
2830
C
3260
C
4230
C
4730
C
4620
C
5340
C
5260
C
5710
C
5690
C
3240
C
2800
C
NRV
7
 In Drum type Boiler Feed water flow control by
Three element controller
 1.Drum level
 2.Ms flow
 3.Feed water flow.
 Drum less Boiler Feed water control by
 1.Load demand
 2.Water/Fuel ratio(7:1)
 3.OHD(Over heat degree)
8
DESCRIPTION SUPERCRITICAL
(660MW)
SUB-CRITICAL
(500MW)
Circulation Ratio 1 Once-thru=1
Assisted Circulation=3-4
Natural circulation= 7-8
Feed Water Flow
Control
-Water to Fuel
Ratio
(7:1)
-OHDR(22-35 O
C)
-Load Demand
Three Element Control
-Feed Water Flow
-MS Flow
-Drum Level
Latent Heat Addition Nil Heat addition more
Sp. Enthalpy Low More
Sp. Coal consumption Low High
Air flow, Dry flu gas loss Low High
DESCRIPTION SUPERCRITICAL
(660MW)
SUB-CRITICAL
(500MW)
Coal & Ash handling Low High
Pollution Low High
Aux. Power
Consumption
Low More
Overall Efficiency High
(40-42%)
Low
(36-37%)
Total heating
surface area Reqd
Low
(84439m2
)
High
(71582m2
)
Tube diameter Low High
10
DESCRIPTION SUPERCRITICAL
(660MW)
SUB-CRITICAL
(500MW)
Material / Infrastructure
(Tonnage)
Low
7502 MT
High
9200 MT
Start up Time Less More
Blow down loss Nil More
Water Consumption Less More
11
12
I ) Higher cycle efficiency means
Primarily
– less fuel consumption
– less per MW infrastructure investments
– less emission
– less auxiliary power consumption
– less water consumption
II ) Operational flexibility
– Better temp. control and load change flexibility
– Shorter start-up time
– More suitable for widely variable pressure operation
13
ECONOMY
Higher Efficiency (η%)
•Less fuel input.
•Low capacity fuel handling system.
•Low capacity ash handling system.
•Less Emissions.
Approximate improvement in Cycle
Efficiency
Pressure increase : 0.005 % per bar
Temp increase : 0.011 % per deg K
THANK YOU

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SEMINAR ON SUPER CRITICAL BOILER....SAMRIDDHA SHIL.....S@S

  • 1. PRESENTED BY SAMRIDDHA SHIL MECHANICAL ENGINEER 1 GARGI MEMORIAL INSTITUTE OF TECHNOLOGY
  • 2. 2 What is Supercritical Pressure ? Critical point in water vapour cycle is a thermodynamic state where there is no clear distinction between liquid and gaseous state of water. Water reaches to this state at a critical pressure above 22.1 MPa and 374 o C.
  • 3.  1 - 2 > CEP work  2 – 2s > Regeneration  2s - 3 > Boiler Superheating  3 – 4 > HPT expansion  4 – 5 > Reheating  5 – 6 > IPT & LPT Expansion  6 – 1 > Condenser Heat rejection 3
  • 4. 4 AbsoluteAbsolute PressurePressure (Bar)(Bar) SaturationSaturation TemperatureTemperature ((oo C)C) Latent HeatLatent Heat (K J/Kg.)(K J/Kg.) 5050 150150 200200 221221 264264 342342 366366 374374 16401640 10041004 592592 00 VARIATION OF LATENT HEAT WITH PRESSURE
  • 5. 5 Supercritical Boiler Water Wall Rifle Tube And Smooth Tube
  • 6. From CRH Line From FRS Line Boiler Recirculation Pump Economizer Phase 1 Economizer Phase 2 LTRH LTSH 4430 C FRH Platen Heater Mixer Header FSH To HP Turbine To IP Turbine Separator Bottom Ring Header 2830 C 3260 C 4230 C 4730 C 4620 C 5340 C 5260 C 5710 C 5690 C 3240 C 2800 C NRV
  • 7. 7  In Drum type Boiler Feed water flow control by Three element controller  1.Drum level  2.Ms flow  3.Feed water flow.  Drum less Boiler Feed water control by  1.Load demand  2.Water/Fuel ratio(7:1)  3.OHD(Over heat degree)
  • 8. 8
  • 9. DESCRIPTION SUPERCRITICAL (660MW) SUB-CRITICAL (500MW) Circulation Ratio 1 Once-thru=1 Assisted Circulation=3-4 Natural circulation= 7-8 Feed Water Flow Control -Water to Fuel Ratio (7:1) -OHDR(22-35 O C) -Load Demand Three Element Control -Feed Water Flow -MS Flow -Drum Level Latent Heat Addition Nil Heat addition more Sp. Enthalpy Low More Sp. Coal consumption Low High Air flow, Dry flu gas loss Low High
  • 10. DESCRIPTION SUPERCRITICAL (660MW) SUB-CRITICAL (500MW) Coal & Ash handling Low High Pollution Low High Aux. Power Consumption Low More Overall Efficiency High (40-42%) Low (36-37%) Total heating surface area Reqd Low (84439m2 ) High (71582m2 ) Tube diameter Low High 10
  • 11. DESCRIPTION SUPERCRITICAL (660MW) SUB-CRITICAL (500MW) Material / Infrastructure (Tonnage) Low 7502 MT High 9200 MT Start up Time Less More Blow down loss Nil More Water Consumption Less More 11
  • 12. 12 I ) Higher cycle efficiency means Primarily – less fuel consumption – less per MW infrastructure investments – less emission – less auxiliary power consumption – less water consumption II ) Operational flexibility – Better temp. control and load change flexibility – Shorter start-up time – More suitable for widely variable pressure operation
  • 13. 13 ECONOMY Higher Efficiency (η%) •Less fuel input. •Low capacity fuel handling system. •Low capacity ash handling system. •Less Emissions. Approximate improvement in Cycle Efficiency Pressure increase : 0.005 % per bar Temp increase : 0.011 % per deg K