(2-2014)-19.1-ciclos avanzados de generacion(adc)
DESCRIPTION
CICLOS AVANZADOS DE GENERACION(ADC)TRANSCRIPT
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Advanced gas turbine power cycles
Chris Hodrien
FUEL
INLET
INLET
COMPRESSOR
COMBUSTORS POWER
TURBINE
EXHAUST
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Typical aero-derivative GE LM6000, 40 MW
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Heavy-duty GT (GE9H) 370 tonnes
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GT design convergence
Open-cycle
Efficiency,
% LHV
1960 2004
25
45
40
HEAVY DUTYAERODERIVATIVE
JET -CIVILJET - MILITARY
TECHNOLOGY TRANSFER
GE 9H
ICAD
I.C. ENGINE
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GT schematic
SC PT PT
GEN
EXHAUST
FUEL
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Combined Cycle (CCGT) principle
Cost: +90% (per kW)
Efficiency: +22%
Power: +50%
SC PT PT
GEN
HRSG
STEAM S
GEN 2
EXHAUST
ST
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CCGT: state of the art
• Standard air-cooled GT: 58% LHV, 430 MW (1+1)• GE 9H steam-cooled GT: 60% LHV, 480 MW (1+1)• Nox g’tee (full load, NG) 25 ppm, 10 ppm available,
lower in advanced dev’t • Dry cooling option• Fuel-flexible NG/ distillate oil• Combustors available for syngas (for IGCC) and H2
(for C capture/renewable H2) (some models)– result of extensive combustion R&D investment
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CCGT Plant with “dry” air-cooled condenser
Takasago Machinery Works, Japan 1999 MHI/Westinghouse W701G 1+1
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23MW mobile power plant (GE LM-2500)
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Barge-mounted CCGT -1
Mangalore, India 4+1 CCGT 2490MW on delivery ship
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A) Advanced Combined Cycles (CCGT)
• Better steam bottom cycle:– Multi-pressure– Reheat– CCGT eff’y improved 48 -> (58-60)% LHV in
20 years
• Kalina (ammonia) cycle• Organic Rankine Cycle (ORC) bottoming
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3-pressure/reheat steam cycle(3-admission turbine)
S
IP LP
GEN
HP
HRSGGT
RH
IP LPHP
CONDENSER
RETURN TO HRSG
WATER
DE-AERATOR
Typical pressures for a 3-pressure steam cycle: 40 atm, 16atm, 7atm.
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Kalina Cycle vs. CCGT –cooling curves
CCGT Kalina cycle –
More heat recovered
PINCH
POINT
Area between curves = wasted exergy (potential work)
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B) Advanced simple GT cyclesTargets:• Efficiency improvement:
– “mid-range” generation– better than simple GT (40-50% LHV) at lower
cost and better flexibility than CCGT
• Better part-load efficiency • Better “hot-day” efficiency• Lower NOx• Carbon capture (CCS)??
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Advanced simple GT cycles• Catalytic combustion• Reheat• Steam-cooled GT• Inlet-chilled• Recuperated• Spray-Intercooled (SPRINT)• Intercooled (ICAD)• Steam injection (STIG)• Humid Air turbine (HAT cycle)• Chemically Recuperated GT (CRGT cycle)
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Catalytic Combustion for NOX reduction
Source: Dr J M Rhine
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Reheat GT cycle(ex: Alstom GT24/GT26)
SC PT PT
GEN
FUELFUEL
Cost: +5%
Efficiency: +3%
Power output: +40% Better part-load efficiency +NOx
Allows more fuel to be burned + power gen’d within metal temp. limit
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Alstom GT26 Reheat turbine
FUEL 1
FUEL 2FLAME
AIR
EXHAUST
MAIN AIR
COOLING AIR
HOT GAS PATH
ROTOR (SOLID)
ROTOR BLADES (“BUCKETS”)
FIXED BLADES (“NOZZLES”)
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Steam-cooled GT (GE 9H)
Cost: +10% (per KW)
Efficiency: +2% (in CCGT)
Power: +20%
SC PT PT
GEN
BLR
COOLSTEAM
HOT STEAM
TO STEAMTURBINE
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Inlet chilling 1– evaporation or “micro-fogging”
Cost: +5%
Efficiency: +2%
POWER +20% (AT 35 oC/ dry air)
WATER
SC PT PT
GEN
V
Hot countries: GT power output is lowest at time/season of max. demandIncreases air density + mass flow at low cost-BUT Only works if inlet air is dry
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Inlet air evaporative cooling (fogging)
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Inlet chilling 2 –refrigeration
Cost: +10%
Efficiency: +5%
POWER +20% net (AT 35 oC/ DAMPair)
SC PT PT
GEN
REFRIG. POWER
(5 %)
(OPTIONAL
COLD STORE)
Increases air density +mass flow
Higher cost but still works if inlet air is wet
Uses some of the extra power made
Absorption chilling option [NOT shown] (use exhaust heat, less power)
Option to store chilling from cheap overnight power
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Water Spray Intercooling (SPRINT)
SC PT PT
GEN
WATER
PUMP
Cost: +5%
Efficiency: +0.5%
POWER: +9% Better part-load and hot-day efficiency
Reduces compressor power use
Increases total mass flow like STIG
Must ensure micro-droplets + high purity to avoid blade erosion
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Dry Intercooling (ICAD)(R&D Prototype - GE)
SC PT PT
GENCost: MINUS 25% (per kW)
Efficiency: +5%
POWER: +100% Better part-load and hot-day efficiency
Major new development ($200M R&D costs)
Initiated by CAGT international collaborative project
Very difficult aerodynamic design + stresses
No water needed
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GE LMS-100 ICAD (intercooled)
Source: GE brochure
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GE LMS-100 ICAD (intercooled)-2
Water cooling Air cooling
Source: GE brochure
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Recuperated GT cycle(e.g.: Solar)
SC PT PT
GEN
RECUPERATOR
(HEAT EXCH’R)
Cost: +20%
Efficiency: +5%
Power: -2% Better part-load efficiency
Recuperator is bulky, costly + unreliable (leaks)
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Steam Injection (‘STIG’) cycle
Cost: +30%
Efficiency: +4%
Power: +24% Better part-load efficiency+ NOx
SC PT PT
GEN
BLR
STEAM
“Poor man’s Combined Cycle” (no steam turbine)
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HAT (Humid Air turbine) cycle concept (EPRI)
Cost: +25%
Efficiency: +6%
POWER: +30% Better part-load efficiency +NOx
SC PT PT
GEN
HOT WATER
SPRAY
TOWER
H/E
Recovers more heat (therefore more H2O mass flow boost) than STIG
Avoids boiler insurance+ manning problems
Spray tower is very large (NOT to scale!) + complex H/E system
NOT yet built
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Compressed Air Energy Storage (CAES)
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CAES Features
• 15 min startup from cold• rapid load ramping• Superior part-load efficiency (only 15%
penalty at 25% load)• Uses only 30-40% of normal fuel rate
during gen. Period• Good spinning reserve capability
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Chemically Recuperated Gas Turbine (CRGT cycle)
Cost: +30%
Efficiency: +9%
Power: +30%
Highly advanced R&D concept (complex)
Boiler but no steam turbine
Process expertise required
Prospect for low-cost CO2 removal
SC PT PT
GEN
REF BLR
NG
HYDROGEN
+ STEAM
CO2
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The Joker In The Pack: Carbon Capture + Storage (CCS)
• WILL CCS be required for gas-fired plant, or only for coal ?
• What % CCS required for coal?– c. 90% ?– NG CCGT equivalence (c. 60%)?– Pre-capture (IGCC) or post-capture?
• Post-capture for CCGT: high % eff’y drop for GT (back-pressure)
• Pre-capture: reform NG into H2 +remove CO2 (CRGT cycle) (fully-proven technology elements)– demo should be funded (BP Peterhead debacle)
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Squaring the circle: IGCC• Integrated Gasification-Combined Cycle (IGCC)• Fuels: Coal, pet.coke, heavy resid. oil• Combines resource availability/ low price of solid fuels
with low emissions of gas (“coal cleaning” technique)• Perceived reliability/ complexity/ commercial issues• Cost without CCS: 15-20% higher than PC coal• CCS penalty much lower than for PC, and fully-proven*
“pre-capture” technology– CCS demo’d on full scale at Great Plains, USA since
1997 (>2M tonnes CO2 sold + sequestered) • “The way to go” for coal +CCS new-build for the low-
CO2 era• Gov’t currently only funding PC post-capture demo
option
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IGCC performance• Efficiency 43-45% LHV (and proportionate CO2
reduction if no CCS)• S removal 99+% + saleable product (S or H2SO4)• Proven CO2 removal 85-90+% + saleable product
(CO2 for oil/gas-field EOR)– actual gas volume treated = 1/180th!
• Water use 1/3 - Site independent of large rivers• NOx emissions <1/20th (10-25 ppmv)• Hg emissions –neglig.• Dust emissions (main combustion ) NEGATIVE!• Solid waste – saleable slag aggregate (low leaching) • Liquid waste – small volume, on-site cleanup• Flexible coal/NG feed (startup, peaking, fuel balancing)• Retrofittable to existing PC sites