csp concentrating solar (thermal) power technologies · pdf fileconcentrating solar (thermal)...
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Slide 1
CSPConcentrating Solar (Thermal) Power
Technologies and Challenges
Manuel RomeroIMDEA EnergyMóstoles, Spainhttp://www.energy.imdea.org
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Slide 2
CSPConcentrating Solar (Thermal) Power
Technologies and Challenges
Manuel RomeroIMDEA EnergyMóstoles, Spainhttp://www.energy.imdea.org
Concentrating Solar ThermalElectricity for tomorrow…. and
much more
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Slide 3
Index
1. CSP= STE (Solar Thermal Electricity)2. Dispatchable solar electricity: Storage3. Market deployment4. Technology challenges5. CSP beyond STE SFC6. Conclusions
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Slide 4
Solar Thermal Power Plants: Ambition of bulk power production
Solar time
From storage Solar direct
supply
To storage
From storage
Fixed power
Ther
mal
ene
rgy
to tu
rbin
e
Solar time
Fossilbackup Solar direct
supply
Fossil backup
Fixed power
Ther
mal
ener
gyto
turb
ine
OPTICAL CONCENTRATOROPTICAL CONCENTRATOR
RECEIVERRECEIVER
FOSSIL BACKUPFOSSIL BACKUP
HEAT HEAT STORAGESTORAGE
COLD POINTCOLD POINT
HOT HOT POINTPOINT
WW
OPTICAL CONCENTRATOROPTICAL CONCENTRATOROPTICAL CONCENTRATOROPTICAL CONCENTRATOR
RECEIVERRECEIVERRECEIVERRECEIVER
FOSSIL BACKUPFOSSIL BACKUPFOSSIL BACKUPFOSSIL BACKUP
HEAT HEAT STORAGESTORAGE
HEAT HEAT STORAGESTORAGE
COLD POINTCOLD POINTCOLD POINTCOLD POINT
HOT HOT POINTPOINTHOT HOT
POINTPOINT
WWWW
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Slide 5Maricopa Solar by SES, USA
Archimede Priolo Italy by ENEA
LFC in the Liddell Power plant by Areva, Australia
PS10 solar tower by Abengoa, Spain
Solar Thermal Power Plants: Point focus (3D) Linear Focus (2D)
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Slide 6
Optimization of solar concentration systems
• Stagnation temperature:
0_ dT
d rectot
abs
ambabsT
TTCarnot
*
)(**44
ConcTT ambabs
rec
Carnotrecrectot *_
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Slide 7
-Spain: 1,000 GW grid-connected by end 2011, 2,500 by 2013 and 5,000 by 2020.-US: 4,500 MW under construction. Foreseen 8,000 MW by 2020.-First projects in Italy, Morocco, Egypt, Algeria, United Emirates-New markets in India, China, Australia and South Africa
CSP early markets: Spain and US
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Slide 8
USA: Distribution by technologies
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Slide 9
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Slide 10
CSP: Examples of commercial projects in Spain
Villarrobledo, Cuenca (Infinia)
PS10 and PS20 (Abengoa Solar)
La Dehesa, Badajoz (SAMCA)
Gemasolar (Torresol)
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Slide 11
La Risca, Alvarado
Acciona/ Mitsubishi Corp (Alvarado, Badajoz)
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Slide 12
Acciona/ Mitsubishi Corp (Majadas, Cáceres)
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Slide 13
Acciona/ Mitsubishi Corp (Palma del Rio 1 y 2)
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Slide 14
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Slide 15
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Slide 16
Extresol 1 and 2
Two storage tanks (ø= 36 m, h=14 m)• Storage capacity (h): 7,5h @ 50 MW• Molten salts: 28,000 Metric Tons/• Melting temperature: 221º C• Working range: 291º C - 384º C
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Slide 17
Andasol 1 and 2
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Slide 18
Manchasol 1 y 2
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Slide 19
Renovables SAMCA, S.A. (La Florida, Badajoz)
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Slide 20
Renovables SAMCA, S.A. (La Dehesa, Badajoz)
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Slide 21
PER 2011-2020: Renewable electricity generation in Spain by 2020CSP & PV = 7.4% (about 30,000 GWh/year)
Coal
Oil & non-renewable wastes
Hydropower by pumping Hydropower
w/o pumping
Solar thermal electricity
Solar PV
Biomass, biogasand urban wastes
Waves and Geothermal
Wind (incl. off-shore)
Total Gross Production of Electricity in 2020:
Natural gas (incl. cogeneration)
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Slide 22
Spanish Renewable Energy Plan 2011-2020
Estimation of daily market price
Cost electricity generation
PV RoofPV Ground
Wind off-shoreWind
CSPWind with 2,900 h/year
Year plant start-up
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Slide 23
For large, state-of-the-art trough plants, current investment costs are USD 4.2/W to USD 8.4/W
CSP: Cost(2 GW learning curve)
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Slide 24
CSP markets: starting in 2007 & only 2GW installed
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Slide 25
The Challenge: Cost reduction
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Slide 26
Parabolic troughs or central tower, operating with thermal fluids at relatively modest temperatures, below 400 ºC .
The most immediate consequences of these conservative designs are: the use of systems with efficiencies below 20%
nominal in the conversion of direct solar radiation to electricity,
the tight limitation in the use of efficient energy storage systems,
the high water consumption and land extension due to the inefficiency of the integration with the power block,
the lack of rational schemes for their integration in distributed generation architectures and
the limitation to reach the temperatures needed for the generation processes following thermochemical routes of solar fuels like hydrogen.
Limitations of first-generation CSP
Extresol 1 and 2 (ACS/Cobra)
PS10 and PS20 (Abengoa Solar)
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Slide 27
295 ºC Oil
395 ºC Oil
Steamgenerator
. Deaerator
ReheaterOil expansion vessel
Steam turbine
CondenserG
Sol
ar F
ield
Steamgenerator
. Deaerator
ReheaterOil expansion vessel
Steam turbine
Condenser
Preheater
Superheated Steam (104bar/380ºC)
ReheatedReheated Steam 17bar/371ºC
G
Sol
ar F
ield
Molten salts(hot tank)
Molten salts(cold tank)
Molten salts(hot tank)
Molten salts(cold tank)
Challenge 1: Storage
Trough Technology with heat storage
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Slide 28
Generation of electricity in Spain during 2011 with CSP (GWh)
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Slide 29
Production week 25-31 July
Production July 2011
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Slide 30
Heat storage: Essential to become dispatchable
• 2-tank molten salt storage for central receiver plants.
• Thermocline pebble bed.• Sand or mobile solid material for
air and particle receivers• PCM/ fins storage for saturated
water/steam
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Slide 31
Thermal energy storageChallenge: < 20-30 €/kWhth
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Slide 32
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Slide 33
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Slide 34
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Slide 35
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Slide 36
DESIGN PARAMETERSTotal Reflective Area 285.200 m2
Number of heliostats 2480
Total Area covered by Heliostat Field 142.31 Ha
Thermal output of the Receiver 120 MWt
Tower height 120 m
Heat Storage Capacity (equivalent toturbine operation) 15 hours
Steam Turbine power 17 MWe
Natural Gas Thermal Power 16 MWt
Projected Operative FiguresDirect solar radiation over Heliostats 2062 kWh/m2
Annual Energy sales 96.400 MWhe
Contribution of Natural Gas 15%
Capacity utilization 65 %
CO2 savings 23.000 – 85.000 t/y
Solar Towers and storage: Gemasolar plant
PotenciaSalida
Energía almacén
media-noche
medio-día
Radiaciónsolar
Radiaciónsolar
media-noche
media-noche
medio-día
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Slide 37
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Slide 38
ADVANCED Technological Concepts
Heating air Brayton cycle Solar Fuels and Chemicals
Solid Particles Receivers
Ceramic Receivers
High Pressure and High Temperature
C. Brayton Heat air
Ceramic Receivers
Low Pressure and High Temperature
Heat air
Solarized Stirling engines
with receiver Dish-Striling
CURRENT TECHNOLOGIES
Volumetric air receivers (metallic)
Cycle Brayton Preheating air
Molten Salt
Receivers Cycle Rankine Heat steam
Sodium Receivers
Heating air
Water/Steam Receivers
Cycle Rankine Heat steam
Oil Receivers Heating steam
500
ºC 1000
ºC 1500
ºC
Solar Receiver Outlet Temperature
CURRENT
Challenge 2: Higher efficiencies (high T, new fluids)
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Slide 39
Current R+D activities related to Trough TechnologyNew receiver tube designs
New evacuated receiver tube designs with glass-to-metal welds
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Slide 40
Receivers: More compact, durable and efficient(Efficiency > 85%)
New tubular panel for molten salt receiver (SENER)
0 1000 2000 3000
Cur
rent
Nex
tge
nera
tion
Peak flux on aperture (kW/m2)
VolumetricMolten saltWater-steam
Direct Indirect Particles Tubular Volumetric Fluid - Water Liquid metals Molten Salts Air Average flux (MW/m2) Peak flux (MW/m2)
(0.9) (2.5)
0.1-0.3 0.4-0.6
0.4-0.5 1.4-2.5
0.4-0.5 0.7-0.8
0.5-0.6 0.8-1.0
Fluid outlet temperature (ºC) (2,000) 490-525 540 540-565 (700-1,000)
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Slide 41
gas
inlet
exit
wal
lgas
gas
absorber
tube receiver volumetric receiver
inlet exit
concentrated solar radiation ~ 1000 kW/m
2
concentrated solar radiation ~ 200 kW/m
2
Volumetric receivers: a good example of high T solar absorption
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Slide 42
Volumetric air-cooled receiver
Incident solar flux
ambient air
absorber structur
SiSiC cup
cooling air
orifice
insulation
hot air
Heat transfer area: 255 m2/m3
Efficiency at 750°: 78% Porosity: 50%
Target:• Improve volumetricity• Increase solar flux
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Slide 43
Superheating steam with dual receivers
eSolar Double Cavity
B&W receiver
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Slide 44
Solar receiver: Reliable black-body is the key
Operational range for different solar receivers (Source: A. Kribus)
0
500
1000
1500
2000
0 20 40 60 80 100 120 140 160
Pressure (bar)
Tem
pera
ture
(ºC
)
Volu-metric
Futuredevelopments
Tubular cavity
Tubular external
Trough linear
n Water-steam need to develop super-heating at high solar flux.
n Volumetric should improve volumetric effect without penalizing fluid-dynamics and flux profile flexibility.
n Molten salt should demonstrate long-term availability and increase peak flux
n Particle receivers and falling films still to pass feasibility phase.
n All should accumulate operational experience and long-term endurance tests.
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Slide 45
El heliostato de SenerChallenge 3: Cheaper concentrators
Large areaheliostats
New reflectors
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Slide 4646
The Solar Energy Development CenterSmall heliostats
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Slide 47
Key data on the solar power station PE 2
Manufacturer Novatec SolarProduct name Nova-1
Model28 rows of linear Fresnel collectors,conventional steam turbine equipment and generator
Solar field length 1.000 m
Net aperture area 302,000 m²
Operating temperature Up to 270 °C
Operating pressure Up to 55 bar
Peak thermal output 150 MWth
Peak electrical output 30 MWel
Planned current output 49 GWh/year
Linear Fresnel
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Slide 48
multitowers
Multitower arrays
Challenge 4:Modularity
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Slide 49
Modularity, urban integration
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Challenge 5: Uncertainty DNI
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Methodology
Based upon images of visible channel from geostationary satellites
Genertion of large temporary series
Estimation of DNI from satelliteimages
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MW-Scale High Fux/High Temperature Solar is possible
Central Receiver
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Challenge 6: Solar ChemistryHigh Flux/High T Solar Reactors
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• 1774: Oxygen is discovered by Joseph Priestly (30 cm diameter lens).
• Antoine Lavoisier formulated the theory of combustion.
• Lavoisier built a solar furnace (>1 m diameter), achieving more than 1700ºC and melted Pt.
Solar Furnace of Antoine Lavoisier(Ilustration XVIII century)
Solar Concentration technologies: Solar Chemistry was first!!!!!
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CONCLUSIONS
CSP introduces solar energy to high-value markets on high temperature processes, providing high capacity and dispatchability.
Solar thermal power plants offer a wide portfolio of integration options with heat storage or hybrid operation for massive production of electricity.
First commercial projects already going on in Spain, USA and elsewhere.
Substantial R&D still needed to reduce costs by 60% Solar Fuels & Chemicals the ultimate target.
CSP: