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TEP4115/4120 TermodynamikkTEP4115/4120 Termodynamikk
Kap 9: Gas Power SystemsKap 9: Gas Power SystemsDel 2
Olav BollandOlav Bolland
1
Bolland
Power production in Norway
• National grid: 99.5% hydropower– 27000 MW - 120 TWh/a– Per capita: 6 kW - 27000 kWh/a
• Offshore oil/gas: mechanical power and local gridsg p g– 3000 MW gas turbine power - 10 TWh/a
• Future:Future:– Wind power: 2002-2010 +3 TWh/a– More hydropower: potential YES y p p– acceptance NO– Natural gas power: potential YES
problem is CO2
– CO2 is a hot issue!!
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Bolland
– Dependence on import of coal & nuclear power?
Kraftproduksjon og forbruk i Norgep j g g
150TWh/år
Variasjonsområde
130
140
150
Prod
Produksjon i normalår med produksjonsapparat som i 2000
Variasjonsområde for produksjon
110
120Prod
Forbruk
Forb -kjeler
80
90
100Forb.-kjeler
Normalår
70
80
1975 1980 1985 1990 1995 2000År
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Bolland
Gas Turbines
Fi 9 8 389
Assumptions for the basic gas turbine cycle:Ai id l i th ki fl id th h t
Fig. 9.8, page 389
• Air, as an ideal gas, is the working fluid throughout• Combustion is replaced with heat transfer from an external source
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Bolland
Gas Turbine Applications• Aero Engines (jet, turbofan, turboprop)• Gas Pipelines (compressor driver)• Power plants (generator driver)Power plants (generator driver)• Combined Heat and Power (generator, utilisation of exhaust heat)• Ship Propulsion• Oil/Gas Platforms (generator & compressor driver)• Oil/Gas-Platforms (generator & compressor driver)• Others (emergency backup, desalination)
• 2000: Production value of aero engines larger than for gas turbines for power generation and mechanical driveg p g
• 2001 : Production value of gas turbines for power generation and mechanical drive larger than for aero engines
Annual production value of gas turbines/aero engines: 50 bill. US$
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General Electric LM5000 d k flLaget med utgangspunkt i flymotor
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Bolland
Cutaway diagram of a Westinghouse 501D5A gas turbine
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Siemens V94.2ca. 150 MW,
første gassturbin med lav-NOXNOX = (NO/NO2) = nitrogenoksiderNOX = (NO/NO2) = nitrogenoksider
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Turbin i gassturbin4 t i Si4-trinns, Siemens
1. trinns løpeskovlerp
1. trinns ledeskovler
Ri b kRingbrennkammer(brennerne kan ikkesees bak til høyre)
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Bolland
sees, bak til høyre)
Work closed/open systems
First law for a closed system:First law for an open system (steady-state):
dU2 1
Relating heat to entropy:
Q W U U 1 2
2 2 2
0
Relating heat to entropy:
dUQ W mh mh
dt
2
1
Q T dS
T dS dU PdV
2 2 2
1 1 1
and and
Q T dS dU pdV
T dS dU PdV T dS dH Vdp
2 2 2
1 1 1
T dS dU PdV
Q T dS dU pdV
2 2
1 1
H U pV dU dH pdV Vdp
Q dH V dp
2
2 1 2 11
U U pdV W U U 1 1
2 2
1 1
Q m dh V dp
22
1
W pdV 2
2 1 1 21
2
( ) ( ) 0m h h V dp W m h h
W V dp
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Bolland
1
W V dp
The Brayton Cycley yCycle Analysis:
12W
12
1 2
Wh h
m
233 2
Qh h
m
m
34
3 4
Wh h
3 4h hm
411 4
Qh h
m
Fig. 9.9, page 389
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Bolland
Ideal Brayton Cycley y
Fig. 9.10, page 391
Using Constant Specific Heats, the cycle thermal efficiency is:
11 1
2
1
1 k
kpp
Fig. 9.11, page 394
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Bolland
1p
Ideal Brayton Cycle, different pressure ratios
Fig. 9.12, page 395
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Irreversibilities in a gas turbine cycleg y
Fig. 9.13, page 397
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Regenerative/recuperative Gas Turbinesg p
2
4 2
xreg
h h
h h
Fig. 9.14, page 400
Største gassturbin med rekuperator R ll R WR21 (20 MW)
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Bolland
4 2h her Rolls Royce WR21 (20 MW)Rekuperator benyttes typisk på små GT, 100-500 kW.
Reheat and Intercoolingg
Fig. 9.16, page 404
Alstom GT26/GT24 (277/191 MW, 3000/3600 rpm)er de eneste gassturbiner som benytter reheat.Alstom bruker begrepet ”sequential combustion”.
Reheat, regeneration, and intercooling are most effective Fig. 9.18, page 407
lstom bruker begrepet sequent al combust on .
when used in combination with one another. However, weight limitations (e.g. aircraft
li ti ) ft li it th i
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applications) often limit their usage.
Aircraft Applications
Fig. 9.20, page 414
Turbo Jet Applications, with and without afterburner
Fig. 9.21, page 415
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Turbo jet – with afterburner
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Aircraft Applicationspp< 1000 km/t
< 600 km/t
a) Turboprop, b) Turbofan, and c) Ramjet applications
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Turbofan
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BollandGE90B777-300ER
RakettmotorRomferge; i brun tank: oksygen hydrogen
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Compressible Flows: The Basics
2 1F V Vm
1-D Steady Flow Momentum Equation:
Velocity of Sound, isentropic wave, ideal gas: c kRT
Mach Number:V
Mc
Stagnation Enthalpy:
2Vh h Stagnation Enthalpy:
0 2h h
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Combined Cycle
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Fig. 9.23, page 419
Hvorfor har en kombinert prosesshøy virkningsgrad ?høy virkningsgrad ?
CARNOTlT
T 1
Carnotvirkningsgrad; en kvalitativ beskrivelse av virkningsgrad for en kraftprosessCARNOT
hTTl er temperatur for varmeavgivelse fra prosessenTh er temperatur for varmetilførsel for prosessen
Gassturbin prosess
K bi t
TTh
Th h
s sh
3 2
3 2høy
2
3
4 h h
Gassturbin prosess
TTh
Th h
s sh
3 2
3 2høy
h h4 1
Kombinert prosess
s
Tl
1
2 4
Th h
s sl
4 1
4 1høy
T h h3 2Dampturbin prosess Tl 1
2
3
4
Ts sl
4 1
4 1lav
s
Th
Ts sh
3 2
3 2lav -
2
3
Th h
s sl
4 1
4 1lav
s
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s
Tl 14
s s4 1
Utvikling av virkningsgrad for gassturbin-anlegg
70
Kombinerte gassturbin-/dampturbinanleggFlyderiverte" gassturbiner
60
65 Store industri-gassturbiner
50
55
grad
[%
]
Kombinerte gassturbin-/dampturbinanlegg
40
45
Vir
knin
gsg
"Flyderiverte" gassturbiner
30
35V
Store industri-gassturbiner
1954 1958 1962 1966 1970 1974 1978 1982 1986 1990 1994 1998 2002 200620
25
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1954 1958 1962 1966 1970 1974 1978 1982 1986 1990 1994 1998 2002 2006
Varmegjenvinning fra en eksosgass ved dampproduksjonved dampproduksjon
700
500
600Eksosgasskurve,stigningstall 1/(m*cp)
400
500
atu
r [C
]ra
ture Eksos/
Exhaust
pinch,minste dT i kjel,begrensende fordampprod ksjon
200
300
Tem
per
aT
emp
e Vann/DampWater/steam
fordamper,fordamping ved
dampproduksjon
100
Overheter,stigningstall 1/(m*cp)
fordamping ved konstant temperatur
economiser,stigningstall 1/(m*cp)
0
0 50 100 150 200 250 300 350
Overført varme [MW]H t t f
stigningstall 1/(m cp)
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Heat transfer
Components of a Vapor Power PlantSteam Power Plant
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Rankine Cycley
Turbine: Pump:Turbine:
1 2tW
h h
Pump:
4 3pW
h h
m m
Overall Performance:
Condenser (1 side):Boiler:
1 2 4 3/ /t pW m W m h h h h
h h
2 3outQ
h hm
1 4inQ
h hm
1 4/inh hQ m
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Combined Cycle Power Plant
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Gasskraftverk Kårstø - 420 MW
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Fuel characteristics for CO2-emission2
Fossil fuels consists of the combustible componentsCarbon (C) and Hydrogen (H)
M th C HM ethane: C H1 4
The ratio between carbon and hydrogen gives the amount of CO2
C H O CO H O2 2 2m n mn
mn
4 22 2 2m n
l il t l
m
n
m
n
m
n
4 2
coal oil natural gas
coal oil natural gas
n n n
11 0 5 0 25. . .
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Bolland
Emission of CO2 from fossil fuels
110012001300
kWh e Methane (H/C=4)
Distillate oil (H/C=2)
90010001100
O2 p
er k Lignite (brown coal)
Bituminous coalAnthrasit
600700800
ram
CO
Anthrasit
300400500600
on o
f gr
100200300
Em
issi
o
30 35 40 45 50 55 60 65 70 75 80 85 90 95 100Eff iciency [%]
0
E
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Bolland
Eff iciency [%]
”CO2-fri” gasskraft?Mest kjente teknologiprinsipperMest kjente teknologiprinsipper
CO₂
N₂/O₂
CO₂
s Power
Post-combustion
₂separation
CO₂
s, B
iom
ass
plant
CO₂ compression & conditioning
ShiftH₂ N₂/O₂
CO₂ compression & conditioning
Powerplant
Gasification
CO₂separation
H₂
CO₂
CO/H₂
Nat
ural
Ga
& conditioning
Power CO₂
& conditioningReforming
CO₂
CO/H₂
Coa
l, O
il, N Pre-combustion
Powerplant
O₂N₂
C
Oxy-combustion
Navn/begreper for de tre metodene:1 P t b ti
Air Air separation
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Bolland
1: Post-combustion2: Pre-combustion3: Oxy-combustion (eller oxy-fuel)