solar thermal energy storage technologies
TRANSCRIPT
Folie 1
Hannover, 23.04.2008
Solar Thermal Energy Storage Technologies
Doerte Laing, German Aerospace Center (DLR)
ENERGY FORUM, 10,000 Solar GIGAWATTSHannover, 23. April 2008
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Energy Storage for Concentrating Solar Power Plants
Higher solar annual contributionReduction of part-load operationPower management Buffer storage
Energy storage necessary forsuccessful market implementationof CSP technology
Solar-heat
ElectricityHeat
ENERGIE-SPEICHER
(optional)
KONZENTRIERENDER
SONNENKOLLEKTOR
WÄRMEKRAFT-MASCHINE
Solar
ENERGY -STORAGE
(optional)
CONCENTRATINGSOLAR COLLECTOR
POWER BLOCK
Fossilfuel
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Highly specific design specifications regarding: primary HTF - pressure - temperature - power level - capacity
Storagesystem
ONE single storage technology will not meet the unique requirements of different solar power plants
Thermal Energy StorageChallenges
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Direct activethermal energystorage
Molten salt sensible heat storage
Solid media sensible heat storage
liquid
solid
Heat transfer fluid as storage media
Two tank oil storage
Dual medium storage system
Passive thermal energy storage
phasechange Latent heat storage
Storage concepts for parabolic trough power plantsClassification
Steam Accumulator
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Thermal Energy Storage for CSP Plants Status und Development
Commercially available storage systemsSteam Accumulator2-Tank sensible molten salt storage based on nitrate salts
Alternative materials and concepts tested in lab and pilot scaleSolid medium sensible heat storage - concrete storageLatent heat - PCM storageCombined storage system (concrete/PCM) for water/steam fluidImproved molten salt storage conceptsSolid media storage for Solar Tower with Air Receiver (e.g. natural rocks, checker bricks, sand)
Future focus for CSPHigher plant efficiency => Increase process temperatureNew fluids: steam, molten salt, gas/air
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Steam Discharging
Isolated Pressure Vessel
Liquid Phase
Steam
Steam Charging
Liquid water Charging / Discharging
Charging process:raising temperature inliquid water volume bycondensing steam
Discharging process:generation of steamby lowering pressure insaturated liquid watervolume
→ Buffer storage for peak power
→ Inefficient and economically not attractive for high pressures and capacities
Steam AccumulatorsStorage of sensible heat in pressurized liquid water
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Steam AccumulatorsPS10
Saturated steam at 250°C50 min storage operation at 50% load
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Steam AccumulatorsPS10
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Steam AccumulatorsPS10
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Molten Salt Storage - Solar Two
Storage capacity (3h)1400 t of nitrate salts(60% NaNO3 + 40% KNO3)2 tanks: 12 m Ø, 8 m high
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Molten Salt Storage – Andasol 1
Conventional steam turbineCollector field Molten salt storage
H2ONaNO3-KNO3Syn. Oil
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Molten Salt Storage – Andasol 1
Ø 38,5 m
14 m
292 °C 386 °C
Storage capacity 1010 MWh (7.7h)Nitrate salts(60% NaNO3 + 40% KNO3)
Salt inventory 28.500 tTank volume 14.000 m³6 HTF/salt heat exchangers
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Molten Salt Storage – Andasol 1
Source: ACS Cobra
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Solid media concrete storage
Dual medium indirect storage system with regenerative heat transferPreferred for single phase HTF up to 400/500 °CModular and scalable design from 500 kWh to 1000 MWhEconomic and reliable TESCost target < 20 € / kWh TES capacityFlexible to large no. of sites and construction materials
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2 year operation of 2 modules350 kWh castable ceramic350 kWh concrete
Second generation concrete400 kWh storage moduledeveloped with
Current investment cost~ 30 €/kWh(large scale, 6 h cycles)
Concrete storage is ready for scale-up and demonstration
System integration and operation strategy is an important issue
Solid media concrete storage – Current Status
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18 m
2,6 m
4 m
134 mmBasic storage module
Solid media concrete storage – Storage Design
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Storage Package
Solid media concrete storage – Storage DesignSet-up of storage units
Storage PackageInsulation
50 m
25 m
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Solid media concrete storage – Storage DesignPiping
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50.000 m³ Concrete Storage Material6 h – Storage for 50 MW-Power Plant
Solid media concrete storage Integration into power plant
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Working fluid water/steam:=> Evaporation phase (T=const)
Phase change storage medium=> Melting phase (T=const)
Significant advantage of PCM technology in steam productiondue to constant temperature
Phase Change StorageWhy using Phase Change Material (PCM) ?
spec. enthalpyte
mpe
ratu
re
solid phaseliquid phase
two phasesolid / liquid
spec. enthalpy
tem
pera
ture
pressurized water
superheated steam
wet steam
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Phase Change StorageSelection of Phase Change Materials
0
50
100
150
200
250
300
350
400
100 150 200 250 300 350Temperature [°C]
Enth
alpy
[J/g
]
KNO3
NaNO3NaNO2
KNO3-NaNO3
LiNO3-NaNO3
KNO3-LiNO3
KNO3-NaNO2-NaNO3
LiNO3
0
50
100
150
200
250
300
350
400
100 150 200 250 300 350Temperature [°C]
Enth
alpy
[J/g
]
KNO3
NaNO3NaNO2
KNO3-NaNO3
LiNO3-NaNO3
KNO3-LiNO3
KNO3-NaNO2-NaNO3
LiNO3For industrialprocess heat
For solar power generation
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Approaches to realize PCM with superior thermal conductivity
Finned Tube Designeffective Lamda >10 W/(mK)
solid
liquid
Fluid
solid
liquid
Fluid
Heat transfer coefficient is dominated by the thermal conductivity of the solid PCM
→ Low thermal conductivity is bottleneck for PCM
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On-sun demonstration of a 200 kWh PCM storage
Dimensions: 5 x 0,6 x 0,5 m3 PCM: 2 tons nitrate salt - 120 kg graphite platesMaximum pressure: 40 barCharging/discharging power 100 kWThermal capacity 200 kWhEstimated investment cost: 45 €/kWh th
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from solar field
to power block
from power block
to solar field
concrete storage module PCM storage
module
concrete storage module
A B
C
D
A feed water inlet / outletB liquid water
C saturated steamD live steam inlet / outlet
preheating
evaporation/ condensation
Combined Concrete / PCM Storagefor direct steam generation in parabolic troughs
superheating
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Conclusions
Energy storage is a key issue for CSP
Steam accumulators only economic as buffer storage
Molten salt technology is available, further improvements for costreduction needed
Concrete storage technology is attractive alternative – demonstration in pilot scale needed
PCM storage technology is the most promising technology for DSG plants
Continuous research and development effort is needed especially for higher process temperatures (> 400°C) and for further cost reduction