oxyfuel power plant design - retrofit options for
TRANSCRIPT
Oxyfuel power plant design - Retrofit options for different fuels
Christian Steinmetz, Christian Bergins, Patrick Weckes, Klaus-Dieter Tigges
14th of September, 2011
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Aim of investigation
Retrofit of oxyfuel technology to existing coal fired power stations
Bituminous coal and raw lignite P.S.
Focus on the entire power plant
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The oxyfuel retrofit requires space
Air Separation Unit (in the vicinity of the power plant)
CO2-Processing-Unit
Flue gas recirculation system to adjust the furnace temperature
Auxiliaries, e. g. flue gas cooling
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Customers view
Customers require
Minimum changes on the existing plant
Coal range to remain unchanged
Minimum life cycle costs
operation
maintenance
investment
CO2-storage
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+107.200 m
+100.700 m
+ 7.700 m
+ 1.1375 m
820 MWel / 2106 t/h
Benson® Steam generator
Bituminous coal
Design parameter:
SH: 600 ºC / 280 bar a
RH: 620 ºC / 52 bar a
Bituminous coal - investigated steam generator
sealing air
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Bituminous coal – air operation
steam generator
Forced - draught fan
Primary
DeNOx catalyst
FGD
exhaust gas
preheater flue gas
ID fan
air preheater
over fire air
FD fan
primary air cooler
fuel
burner system
PA fan
mills
air
air
ESP
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Application of the oxyfuel process
How to achieve minimum changes?
Keep
heat transfer in furnace and convective path
furnace exit temperature
flame shape and length
momentum of burner flows
volumetric gas flow after mills
similar to air combustion.
How?
recirculate dry and clean flue gas (extraction after FGC)
a flow of about 75 % ensures the target
Result: No changes on existing components in the boiler house
sealing air
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Oxyfuel process – required measures
steam generator
Forced - draught fan
Primary
DeNOx catalyst
FGD O2
exhaust gas
preheater flue gas
CO2
ID fan
air preheater
over fire air
FD fan
primary air cooler
fuel
burner system
CO2
PA fan
mills
(retrofit components in red)
FGC
CO2- compression
ASU
ambient air
O2-preheater
CO2
vent gas
HP feed water preheater
steam preheater
flue gas bypass
air
air
ESP
Hot gas recirculation
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Flue Gas Temperature
Comparison air combustion / oxyfuel combustion
Water/Steam Temperature
SH 600 C
459 C 325 C
294 C
1306 C
381 C
SH1
SH2
RH2
RH1
SH3
Eco
SH 600 C
444 C 326 C
294 C
RH 620 C
385 C
Air Oxyfuel Air Oxyfuel
RH 620 C
1300 C
CO2-concentration downstream FGC
component
N2
O2
Ar
CO2
concentration [vol.-% dry]
95 vol.-% O2
11.3
4.3
80.2
3.9
99.5 vol.-% O2
10.7
4.4
84.1
0.3
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The reachable CO2-concentration downstream FGC depends on
oxygen excess for combustion
purity of applied oxygen
composition of the used coal
amount of air ingress
Example: • = 1.15
65
70
75
80
85
90
95
0 1 2 3 4 5
air ingress [%]
CO
2 co
nte
nt
aft
er F
GC
[v
ol.-
% d
ry]
O2-purity: 95 vol.-%
O2-purity: 99.5 vol.-%
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Retrofit for bituminous coal - conclusion
Oxyfuel retrofit can easily be done
No major changes on the existing boiler
Slight changes in the overall process
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500 MWel / 1330 t/h
Benson® Steam generator
Raw lignite
Design parameter:
SH: 603 ºC / 293 bar a
RH: 609 ºC / 51 bar a
Raw Lignite - Investigated steam generator
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Oxyfuel retrofit for raw lignite
Water content of used raw lignite is 48 wt.-%
Air mode: flue gas water content of 26.3 vol.-%
avoid further accumulation of water in oxyfuel mode
Recirculation downstream
ESP FGD FGC
40.2 68.1 31.4
H2O content at boiler outlet [vol.-%]
Recirculation after FGC
is mandatory
CO2-Storage
oxygen boiler
CO2-Processing-Unit SOX H2O
vent gas
gas-preheater
ESP FGD FGC raw lignite
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O2
Oxyfuel Operation – Raw Lignite
Forced - draught fan
FGC
CO2
vent gas
CPU
ASU
ambient air
draught
ESP
FGD
exhaust gas
steam generator
ID fan Forced -
draught fan
air preheater
FD fan
burner
flue gas preheater
air ingress
raw lignite
O2-preheater
HP feed water preheater
steam preheater
flue gas bypass
(retrofit components in red)
Hot gas recirculation
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Firing system for raw lignite
Coal is dried with hot flue gas from the end of the furnace
Various points of air ingress
between furnace and hot gas off take
at burners
at coal feeder
at coal mill itself
Typical amount of air ingress is 10 % of total combustion air
hot gas off take
suction shaft
burner
coal mill
air ingress
air ingress
air ingress
air ingress
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O2-purity: 95 vol.-%, • = 1.15
CO2-concentration after FGC depending on leak air ingress
N2 30.4
O2 3.1
CO2
Ar
65.1
1.4
O2-purity: 95 vol.-%, • = 1.15
concentration [vol.-% dry] component
N2 6.2
O2 3.4
CO2
Ar
88.6
1.8
concentration [vol.-% dry] component
10 % air ingress
0 % air ingress
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Retrofit for raw lignite - Conclusion
With a well sealed system the retrofit requires
no major changes on the existing boiler
slight changes on the overall process
The success of an oxyfuel retrofit for raw lignite depends on the amount of air ingress.
CPU, ASU, O2 preheater and respective ducts
flue gas cooler
cooling system
O2 / flue gas mixing
flue gas recirculation duct and connection to existing duct work
hot gas recirculation at GGH
fan modification
bypass heat exchanger for GGH
heat transfer system to feed water preheating
CO2 seal gas for mills to replace air
pure oxygen to FGD to replace air
CO2 for NH3 atomizing upstream of catalyst
I & C adaptation
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Retrofit of a hard coal unit – New components and modifications
Retrofit of a hard coal unit – Unchanged components
• boiler pressure part
• coal handling system (except seal gas)
• burners and p.f. lines
• duct work (except junction to flue gas recirculation and O2 supply)
• turbine and steam extraction lines
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