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Thermal energy storage using rocks, from Paleolithic to CSP technologies.
Speaker: Pr Xavier Py
Col. : Régis Olives, Vincent Goetz, Quentin Falcoz, Najim Sadiki
Doc. : A. Meffre, A. Kere, G. Dejean, J.F. Hoffmann, N. Calvet, T. Nahhas
PROMES laboratory
UPR 8521 CNRS
University of Perpignan Via Domitia
AMREN-2 E-MRS
EURO-MEDITERRANEAN COOPERATION ON RESEARCH & TRAINING IN SUN BASED RENEWABLE ENERGIES (EUROSUNMED)
Introduction : the PROMES lab UPR 8521 CNRS UPVD
At a glance
created 43 years ago by Felix Trombe,
170 persons involved,
50 PhD students,
the largest solar furnace of the world,
a CSP tower power plant at pilot scale.
Activities
Materials for energy under extreme conditions
Concentrated Solar processes and components
Alternative fuels, waste and pollutants
Space issues (Mars)
4 MW
560°C
ancestor of Gemasolar
Thermal Energy Storage :
one of the major distinctive advantage of CSP before other Renewable Energies
- ditpatchability
- process optimization
- process protection
Introduction : needs in thermal energy storage in CSP
GEMASOLAR
Granada Spain
2011
20 MWe
15h TES
NaNO3/KNO3
ANDASOL
Sevilla Spain
2006
50 MWe
7h.5 TES
28 000 t
NaNO3/KNO3
50 MWe
625 collecteurs (12m long, 6m ouverture)
260 millions euros
195 hectares
152 000 tonnes CO2/an
50 MWe - 7.5 h storage
(28 000 t molten salt binary nitrate)
291 – 384 °C
A mix between SEGS and Themis/Solar Two
ANDASOL Granada Spain 2009 : today’s « standard » for trough CSP
Introduction : thermal energy storage in CSP Solar trough CSP plants
Gemasolar 2011: 15h of TES 20 MWe, 195 ha, 230 M€
DT 290 to 565°C
Crescent Dune USA 110 MWe (2015)
500 GWh/y
The first industrial 24h/day Solar CSP Tower
Introduction : thermal energy storage in CSP Central receiver CSP approach
Effects of TES on financial issues:
Increase in investment costs by the added TES
and the increased size of the solar field
The whole energy cost changes only marginally.
The main merit of the TES:
Not to reduce the cost of electricity
But increase in plant capacity factor
Supply of base-load power competing with fossil-fuel
TES in a state of the art CSP plant - Financial issues
50 MWe
200 M€
J. J. Burkhardt, G. a Heath, and C. S. Turchi,
Life cycle assessment of a parabolic trough concentrating solar power plant and the impacts of key design alternatives.
Environmental science & technology, vol. 45, no. 6, pp. 2457–64, Mar. 2011.
GHG
TES 19.3%
CED
TES 18%
ANDASOL like
Trough CSP
103 MWe
6.3 h TES :
Mined nitrate salt
TES in a state of the art CSP plant - Environmental issues
0.19
0.028
0.17
0.0019
0.0098
0.4
19.5%
36%
9.4%
1.5%
89.8%
Cumulative
Energy demand
12
1.7
10
0.12
2.1
26
23%
38%
1%
1.6%
32%
Green House Gaz
Emissions
TES in a state of the art CSP plant - Material availability
today 0.8 Mt
About 800 €/t
Before CSP needs
10% CSP in 2050 :
9 to 21 Mt/year
of nitrates !
The Natural Nitrates from Chile to keep as HTF but not as TESM
133 Mm3 wastes
417 km² polluted surface
> 100 ghost plants
(P. Marr 2007)
Raw Material availability : the nitrate salts
France: Les Eyzies 32.000 BP
West North America 10.500 BP
1. Thermal capacity of stones
2. Management of fast fuels
3. Steam or boiling water production
Iterative process
with TES !
Paleolithic heritage: pyrotechnologies using stones as TESM
700 °C
Thermal behaviour of stones: Basalt stone
Tamar Nahhas
Non reactive stone
Stable up to 800°C
Thermal behaviour of stones: Basalt stone
Tamar Nahhas
heating
cooling
Pyrotechnologies at Paleolithic:
72 000 BP – 20 000 BP South Africa and West Europe
Intentional heating treatments of flint stones
to help or even allow flint-stone tools manufacturing.
High skills in controled heating treatment…
Observed from 1908 but …
Used protocoles: Mercieca 2008
Involved mechanisms : Schmidt et al. 2012
Still preliminary studies, need deeper efforts
Solutrean (- 20.000)
Boulazac in Dordogne
« Feuilles de laurier »
shaped in
heat treated flints
P2 Alternative approach: reactive natural rocks on the paleolithic side
Research Prg CNRS « Paleostock »
•SA: Salinelles (Gard)
•ML: St Martin de Londres (Hérault)
•CG: Costières du Gard - St Gilles (Gard)
•NS: Narbonne-Sigean- Presqu'il du Doul (Aude)
Reactive stone
TESM below 400°C
H2O free
Open
porosity Conversion
silanols
Fracturation
H20
departure
Thermal behaviour of unstable stones: flint stone P2
Tamar Nahhas
Thermal behaviour of unstable stones: flint stone P2
Rather high values
Basalt : 2 at 400°C
Great range
Test at pilot scale: Basalt and Quartzite 325 kg
Parameter PROMES-CNRS
Energy 8.3 kWhT
HTF Rapeseed oil
TESM Quartzite rock
Tank height 1.8 m
Tank diameter 0.4 m
Porosity 0.41
Particles diameter 0.04 m
Volume 0.25 m3
Mass 325 kg
High temperature 210°C
Low temperature 160°C
Basalt: igneous rock Quartzite: metamorphic rock
JF Hoffmann
PhD 3 dec. 2015
P2
STORAGE CAPACITY : density recycled ceramics versus rocks
E.C. Robertson Thermal properties of rocks, Open File Report 88-441, 1988,
U.S. Department of the Interior, Geological Survey. Rocks properties :
ACW ceramics FAW ceramics
0 500 1000 1500 2000 2500 3000 3500 4000
Wollastonite CaSiO3
Augite Ca(Mg Fe Al)(AlSi)2O6
Gehlenite Ca2Al2SiO7
Spinel MgAl2O4
Granite (Igneous)
Quartz mica schist (metamorphic)
Shale (sedimentary)
ACW Ceram
MSWIFA Ceram
r = 3100 kg/m3
r = 2975 kg/m3
rocks
min
era
ls
Comparison with recycled ceramics in terms of density
Comparison with recycled ceramics in terms of Cp
STORAGE CAPACITY : Cp
0
200
400
600
800
1000
1200
0 250 500 750 1000
Cp
(J/k
g K
)
T (°C)
ACW ceramics
785 - 1072
MSW FA
0
1
2
3
4
5
6
7
0 200 400 600 800 1000 1200 1400
Co
nd
uct
ivit
y W
/(m
K)
T (°C)
poor feldspar
rich in feldspar
quartzite
poor in quartz
carbonates
clastic sediments
conduc dom
radiat dom
ACW Ceram
MSWIFA Ceram
CFA Ceram
THERMAL CONDUCTIVITIES : recycled ceramics versus rocks
ACW ceramics
l 1.5 W/(m K)
Plutonic rocks
Metamorphic rocks
Sedimentary rocks
Volcanic rocks
C. Clauser, E. Huenges. Thermal conductivity of Rocks and Minerals. 1995,
A Handbook of Physical Constants, AGU Reference Shelf 3, the Americal Geophysical Unions. Rocks properties :
Comparison with recycled ceramics in terms of thermal conductivity
Calcium carbonates
wastes : shell, rocks
BIC BF : Ca(OH)2 from
acethylene industry
Coal Fly Ash
SiO2: 45%
Al2O3: 22%
CaO: 6%
SiO2: 45% to 3%
Al2O3: 5 to 30%
Fe203 : 15 to 70%
Laterites
Area of
Expected ceramics
Formulation :
To get a specific ceramic
Elaboration:
To control the internal structure and
then, the expected properties
Technological bottlenecks and next challenges
K. N'TSOUKPOE, Y. K AZOUMAH , E. W RAMDE, Y. A FIAGBE P. NEVEU, X. PY, M. GAYE ; A. JOURDAN.
Integrated design and construction of a micro central tower power plant. (2015) Energy for Sustainable Development, 31 (2016) 11-13..
Rocks :
High acceptability
Some directly available
Some need initial stabilisation
Mostly restricted to granular bed
Recycled ceramics :
Sustainable issue preserving still on site natural resources
Controled structure (refractory behavior)
Complex geometry for process optimization
Self supported storage packing
Needs related industrial facilities and costs
Embodied energy for elaboration (E pay back time < 2 years)
Comparison between rocks and recycled ceramics
Corrugated TES plate of TESM from metalurgic slag Flat TES plate made of vitrified ACW
P3
Thank you for your attention