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Title: super critical boiler


1
  • SUPERCRITICAL BOILER

By Ashvani Shukla CI BGR ENERGY
2
Introduction to Supercritical Technology
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 oC.
3
Rankin Cycle Subcritical Unit
  • 1 - 2 gt CEP work
  • 2 - 3 gt LP Heating
  • 3 - 4 gt BFP work
  • 4 - 5 gt HP Heating
  • 5 6 gt Eco, WW
  • 6 7 gt Superheating
  • 7 8 gt HPT Work
  • 8 9 gt Reheating
  • 9 10 gt IPT Work
  • 1011 gt LPT Work
  • 11 1 gt Condensing

4
Rankine Cycle Supercritical Unit
  • 1 - 2 gt CEP work
  • 2 2s gt Regeneration
  • 2s - 3 gt Boiler Superheating
  • 3 4 gt HPT expansion
  • 4 5 gt Reheating
  • 5 6 gt IPT LPT Expansion
  • 6 1 gt Condenser Heat rejection

5
VARIATION OF LATENT HEAT WITH PRESSURE
Absolute Pressure (Bar) Saturation Temperature (o C) Latent Heat (K J/Kg.)
50 150 200 221 264 342 366 374 1640 1004 592 0
6
Nucleate boiling is a type of boiling that
takes place when the surface temp is hotter than
the saturated fluid temp by a certain amount but
where heat flux is below the critical heat flux.
Nucleate boiling occurs when the surface
temperature is higher than the saturation
temperature by between 40C to 300C.
Departure from Nucleate Boiling
7
Supercritical Boiler Water Wall Rifle Tube And
Smooth Tube
8
Natural Circulation Vs. Once Through System
9
To HP Turbine
5710C
To IP Turbine
5690C
Mixer Header
5340C
4230C
5260C
4620C
Separator
FRH
4730C
FSH
Platen Heater
LTSH 4430C
From CRH Line
3260C
LTRH
3240C
NRV
2830C
From FRS Line
2800C
Economizer Phase 1
Economizer Phase 2
Boiler Recirculation Pump
Bottom Ring Header
10
Feed water control
  • 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(71)
  • 3.OHD(Over heat degree)

11
Difference of Subcritical(500MW) and
Supercritical(660MW)
12
COMPARISION OF SUPER CRITICAL SUB CRITICAL
DESCRIPTION SUPERCRITICAL (660MW) SUB-CRITICAL (500MW)
Circulation Ratio 1 Once-thru1 Assisted Circulation3-4 Natural circulation 7-8
Feed Water Flow Control -Water to Fuel Ratio (71) -OHDR(22-35 OC) -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
13
Continue..
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
14
Continue..
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

15
Water Wall Design
16
WATER WALL ARRANGEMENT
  • Bottom spiral top vertical tube furnace
    arrangement
  • Once through design feature is used for boiler
    water wall design
  • The supercritical water wall is exposed to the
    higher heat flux
  • Spiral tube wall design (wrapped around the unit)
    with high mass flow velocity of steam/water
    mixture through each spiral
  • Higher mass flow improves heat transfer between
    the WW tube and the fluid at high heat flux.

17
SPIRAL VS VERTICAL WALL
  • VERTICAL WALL
  • SPIRAL WALL
  • Less ash deposition on wall
  • Less mass flow
  • More number of tubes
  • More boiler height for same capacity
  • No uniform heating of tubes and heat transfer in
    all tubes of WW
  • More ash deposition
  • More fluid mass flow
  • Less number of tubes
  • Less boiler height
  • Uniform heat transfer and uniform heating of WW
    tubes

18
Furnace Arrangement
SPIRAL TYPE
VERTICAL TYPE
19
Supercritical Sliding Pressure Boiler Water Wall
Design Comparison of Vertical Wall and Spiral Wall
20
(No Transcript)
21
Ash accumulation on walls
22
Super Critical Boiler Materials
23
Advanced Supercritical Tube Materials (300
bar/6000c/6200c)
24
Material Comparison
Description 660 MW 500 MW
Structural Steel Alloy Steel Carbon Steel
Water wall T22 Carbon Steel
SH Coil T23, T91 T11, T22
RH Coil T91,Super 304 H T22, T91,T11
LTSH T12 T11
Economizer SA106-C Carbon Steel
Welding Joints (Pressure Parts) 42,000 Nos 24,000 Nos
25
Steam Water Cycle Chemistry Controls
26
S. No. Parameter Sub Critical Super Critical
1 Type of Boiler water treatment LP and HP dosing. Or All Volatile Treatment (Hydrazine Ammonia) No HP dosing Combined water treatment (CWT).
2 Silica lt 20 ppb in feed water and steam, lt 250 ppb in boiler drum Standard value lt15 ppb in the cycle Expected value lt10 ppb in the cycle
3 pH 9.0 - 9.5 for feed, steam condensate, 9.0 10.0 for Boiler drum 9.0 9.6 for AVT(All volatile treatment) 8.0 9.0 for CWT(Combine water treatment)
4 Dissolved Oxygen (DO) lt 7 ppb for feed. lt 7 ppb for feed in case of AVT 30 150 ppb for feed in case of CWT
5 Cation (H) Conductivity lt0.20 µS/cm in the feed steam cycle Standard value lt0.15 µS /cm in the cycle Expected value- lt0.10 µS /cm in the cycle
6 (CPU) CPU is optional CPU is essential for 100 flow.
7 Silica and TDS control By maintaining feed water quality and By operating CBD Blow down possible till separators are functioning (upto 30 load).
27
Advantages of SC Technology
  • 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

28
ECONOMY
Higher Efficiency (?)
  • 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

29
Increase of Cycle Efficiency due to Steam
Parameters
30
Sub. vs. Supercritical Cycle Impact on Emissions
31
Challenges of supercritical technology
  • Water chemistry is more stringent in super
    critical once through boiler.
  • Metallurgical Challenges
  • More complex in erection due to spiral water
    wall.
  • More feed pump power is required due to more
    friction losses in spiral water wall.
  • Maintenance of tube leakage is difficult due to
    complex design of water wall.
  • Ash sticking tendency is more in spiral water
    wall in comparison of vertical wall.

32
THANK YOU
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