4- CFBC
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Transcript of 4- CFBC
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Presentation on CFBC Technology
by
CETHAR VESSELS (P) LTD
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COMPARISON WITH OTHER TECHNOLOGIES
PULVERIZED FIRING FLUIDIIZEDBED FIRING
VELOCITY 2-3 m/ sec 5 10 m/sec 1.5 3 m/sec 4.5-6.5 m/sec
FUEL FEED SIZE 37 mm X 0 200 microns 6 mm 12 mm X 0
FURNACE TEMP. 1150- 1450 C 1250- 1600 C 850- 950 C 850- 950 C
COMBUSTIONEFFICIENCY %
85-90 99 95-96 98-99
GAS
FUEL
AIR ASH
STROKER FIRING
(FIXED BED)
ASH
(ENTRAINED BED)
GAS
AIR
FUEL
ASH
FUEL & SORBENT
AIR
GAS
BFB
ASHAIR
FUEL & SORBENT
AIR
CFBGAS
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Typical CFBC Boiler
Typical CFBC Boiler
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Design Features of CVPLs CFBC Boiler
Gas tight Water cooled membrane wallconstruction for furnace
Lower Combustor with Refractory lining
Water cooled hot cyclone separator with insiderefractory lining
Entire recirculation loop i.e., Return leg, LoopSeal & Down Chute are made of membrane Panel
with refractory lining
Elimination of maintenance prone expansionjoints at the inlet of Cyclone, inlet & outlet ofLoop Seal
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Design Features of CVPLs CFBC Boiler
The Convective heat transfer banks such as Superheater & Economizer are located in downstreamof Cyclone separator to avoid erosion
Wing wall heat transfer surface is provided in theupper furnace to balance the heat pick-up
between Evaporator and Super heater, if required
Specially designed non-mechanical Loop Seal
Non-mechanical flow control device for regulation
of bed ash removal
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ADVANTAGES OF CFBC OVER AFBC Higher boiler efficiency
Higher combustion efficiency Compact arrangement Adaptability for high capacity utility boilers Suitable for firing low grade fuels Effective sulphur retention
Eco-friendly with low air pollution Less fuel feed points results in simple
arrangement Fuel flexibility Better Turndown ratio No Bed Coil and Bed Super heater Coil and hence
Less Maintenance and higher availability.
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ADVANTAGES OF CFBC OVER PC FIRED
BOILER
High fuel flexibility
Accepts low grade fuel with high ash content
Accepts higher fuel size (up to 12 mm)
No milling plant and related maintenance
Effective Sulphur retention (up to 97%)withlimestone addition under optimum condition.
No FGD for Sulphur retention
Low Nox emission due to low furnace
temperature and staged combustion Oil firing is required only for start-up
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SOx AND NOx CONTROL
Lower Sox emission due to Higher recirculation of sorbant Higher volume of fluidized bed Higher turbulence in the bed Finer sorbant particle Better interaction of sorbant with air /
sulphur
Lower Nox emission due to - Low furnace operating temperature
Staged combustion(Primary and Secondary air introduced in
combustor at different elevation)
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Grid Nozzles
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Refractory Lining Protects Furnace
Separator Tubes
Thin Studded RefractoryLining Provides:
Reduced WeightReduced Maintenance
Studs Stabilize RefractoryCooler Refractory Reduces Erosion
Rates
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Furnace Tube Design Eliminates Erosion
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Vertical Super Heater/ Evaporator Panels
Resist Erosion
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% MCR LOAD vs SH STEAM TEMP.
440450
460
470
480
490
500
510
520
530
540
30 40 50 60 70 80 90 100
% MCR LOAD
SH
STEAMT
EM
P.DEG.
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CFBC - can accommodate a wide Range of Fuel Properties
Range of Fuel Properties for CFBs
Moisture Up to 60 % ( Brown coal, Peat, Sludge)
Ash Up to 76 % ( Waste Anthracite )
Sulphur Up to 10 % ( Waste Bituminous Petroleumcoke )
Volatile Down to 1% ( CHAR )
HHV Down to 1400 Kcal/Kg ( CHAR )
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CFBC - REFERENCE LIST
S.No CUSTOMER NAME CAPACITYKG/HR
PRESSUREKG/SQ.CM
STEAMTEMP.DEG.C
FUELS STATUS
01. SHRI RAMRUPAI BALAJISTEELS LTD, DURGAPUR,W.B.
170,000 86 515+/-5 Char(GCV-1700Kcal/Kg with 70%Ash) + BF Gas.
U.E
02. ORIENT CEMENT, DEVAPUR,ANDHRA PRADESH
114,000 88 520 +/- 5 Coal MiddlingDry cake + Rice Husk /Wood Chips.
U.E
03. ORIENT CEMENT, DEVAPUR,ANDHRA PRADESH
114,000 88 520 +/- 5 Coal MiddlingDry cake + Rice Husk /Wood Chips.
U.E
04. SAKTHI SUGARS LTD,TAMILNADU.
110,000 108 510 +/- 5 Bagasse + Coal +Distillery effluent.
U.E
05. ACC LIMITED, WADI 110,000 67 485+/-5 Coal Middling & Coal U.E
06. ACC LIMITED, WADI 110,000 67 485+/-5 Coal Middling & Coal U.E
07. BINANI CEMENT LTD,
SHIROHI, RAJASTHAN.
92,000 87 510+/-4 Barmer Lignite
Pet coke, Indian CoalImported Coal
U.E
U.EUNDER EXECUTION
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CFBC - REFERENCE LIST
S.No CUSTOMER NAME CAPACITYKG/HR
PRESSUREKG/SQ.CM
STEAMTEMP.
DEG.C
FUELS STATUS
08. BINANI CEMENT LTD,SHIROHI, RAJASTHAN.
92,000 87 510+/-4 Barmer LignitePetcoke, Indian CoalImported Coal
U.E
09. SHREE CEMENTS LTD, BEWAR,RAJASTHAN.
85,000 88 520+/-5 PetcokeResidue (Fly ash fromAFBC)
U.E
10. SHRI RAMRUPAI BALAJISTEELS LTD, DURGAPUR,W.B.
85,000 86 515+/-5 Char(GCV-1700Kcal/Kg with 70%Ash) + BF Gas.
U.E
11. ACC LTD, BARGARH. 67,000 67 485+/-5 Coal Middling U.E
12. ACC LTD, BARGARH. 67,000 67 485+/-5 Coal Middling U.E
U.EUNDER EXECUTION
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FUELS CONSIDERED FOR CETHARs CFBC
100 % Char (GCV =1750 Kcal/kg)
100% Petcoke (GCV=7850 Kcal/kg &
10% sulphur)
100% Washery rejects ( ash=70%)100% Lignite ( M=50% max)
100% Indian Coal
100% Imported Coal
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OTHER FUELS (PARTIAL)
Bagasse
Fly ash residue from BFBC boilers
Distillery Effluent
Blast furnace gas
Wood chips
Paper Sludge
Rice Husk
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Thank You