Materials for Energy[PHY563]
IV: Electrochemical Energy Materials & Catalysis
20/01/2021
Jean-François Guillemoles,
Nathanaelle Schneider
Objectives and outline
• Energy conversion and storage
• Basics of electrochemistryo Definitionso Electrochemical reaction driving forceo Ionic conduction
• Basics of catalysiso Key notions: activation energy, catalytic species, activity, selectivity, mechanismo Significance and main applications
• Applications:o Materials for supercapacitorso Materials for batteries (Insertion and conversion materials, tutorial 10/02)o Materials for fuel cells (H2, 10/02)o Related issues : Corrosion ( 12/02) , Photoelectrochemistry, Electrocatalysis ( tutorial)
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5
Energy mix evolution and perspectives
Source : GMO Solar Power Europe 2016
Increasing share of renewables
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Energy consumption – Necessity of storage
Source : https://www.rte-france.com/fr/eco2mix/eco2mix-consommationFluctuating demand
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Energy storage
Mostly PSH
• Heat storage
• Solar thermal
• Molten salts
• Phase Change Materials
• Mechanical storage
• PSH - Pumped Storage Hydroelectricity
• CAES - Compressed Air Energy Storage
• Flywheels
• Electrochemical storage
• Supercapacities
• Batteries
How would you store electricity?
• Types of electrochemical storage you know?
• Can you estimate the energy contained in a cell?
• Its power?
• What is it that you don’t know/ don’t understand about electrochemicalstorage?
o Principles
o Material issues
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Key figures
Source: Fundamentals of Materials for Energy and Environmental Sustainability, Edited by D. Ginley, D. Cahen
• Capacitor - electrical energy stored as surface charge
• Battery - electrical energy stored as chemical energy
• Fuel cell = battery where fuel is supplied at one electrode and the oxidant at the other
SUPERCAPACITORS
Invariant electrolyte and electrodes
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What is the driving force?
How much energy can be stored?
What are the issues?
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Supercapacitors
Source : www.storagealliance.org
Solid-state capacitor(conventionnal)
EC electrochemical capacitorHigh surface area electrode + liquid electrolyte
• No electrochemical reactions
• Charges are accumulated at the material surface through the double layer (EDL)
• EDL
Variation of electric potential near a surface, interfacial field
Several descriptions : Helmholtz (1853) > Marcus (Nobel, 1992)
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EDL – Electrical Double Layer
Debye length (Debye radius) λD
= measure of charge carrier net eletrostatic effect in a solution
and how far it persists
DL Diffuse layer – coulombic interaction + thermal motion, electrically screening the first layer
First layer – surface charges
Supercapacitors
• Electrode materialso Optimum pore size to maximize the capability of the electrolyte
o Inputs of material science, nanosynthesis, simulation and modeling
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Supercapacitors
• No structural changeo Much longer lifetimes (millions of cycles), low maintenance
o Higher rate capabilities, almost instantaneous > repetitive fast applications (braking, acceleration)
• Only surface o Limited energy storage capability (0.1 – 1 Wh./kg)
o Variation of the voltage
• High cost installation
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How to make a battery?
• What are the basic ingredients in a battery?
• What are the desired properties of each component?
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Batteries
Ancient technologies with new materials
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1899« Jamais contente »
1920Wireless communication
TodayTesla roaster
TodayWireless communication
Batteries
Evolution of batteries
PHY563 – N. Schneider 22
Positive electrode
Negative electrode
electrolyte
e-
2020 Many systems Commercial battery types , sodium-sulfur, redox flow
Quite costly for large scale, stationary applications ~ $ 1000/kWh
Difficulties with large power/long term storage /Cyclability => solid state reactions
Lead battery still cheapest
Batteries
Commercial applications
1991LiCoO2/Graphite
2005LiCoO2/Sn-Co-C
Nano-negative
2006LiFePO4/Graphite
Nano-positive
2004Li(Co, Mn,Ni)O2/Graphite
+20%Volumic energy
4 times more powerfull
+60%Mass energy
Very rapid industrial applications
POTENTIAL (ΔE, Volt)Nature of the redox coupleExtent of reaction
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Batteries
Tarascon, cours Collège de France (2011)
Number of exchanged electric charges (Coulombs)
POTENTIAL potential : choice
of redox couple
CAPACITY capacity: system exchanging more than 1 electron
CAPACITY (Q, Coulomb, Faraday, Ah)Nature of the redox coupleQuantity of atoms
Nernst equation
Chemical and electrochemical engines
A chemical reactioncan be separated in 2 electrochemical half
reactions
• For one mole
• At each electrode:
Electrode equilibrium: Nernst
• Electric potentials of solution and metal:
• Ideal Solution
• Nernst law:
Losses
(1) Activation overpotential : Potential barrier of redox reaction => reduced by additional potential
(2) Concentration overpotential: Concentration depletion at electrode = > local potential shifted from equilibrium
(3) Conduction overpotential : Ohmic drop
PHY579 – N. Schneider 28
Issues
• Electrode overpotential: reversibility
• Series resistance : power efficiency
• Cyclability and stability (See Lecture on material degradation)
• LCA
Material issues
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Batteries
• Why Lithium batteries?
PHY563 – N. Schneider 31Tarascon, cours Collège de France (2011)
> Small ionic radius
rapid diffusion >> Power
> Works in aqueous medium
>> Thermodynamic limit at 1.2 V
> Lightest metal (6.9g), d= 0.53g.cm-3
> Most electropositive element
>> ΔE 3 – 4V
> High chemical reactivity (water)
>> Organic electrolytes (non aqueous)
Highest energy mass density
BATTERIES TYPE I : LITHIUM TECHNOLOGIES
Invariant electrolytes/redox electrodes
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Li - metal
PHY563 – N. Schneider 33Tarascon, cours Collège de France (2011)
Li-metal > negative electrode = metal Li
Discharge:TiS2 + e- + Li+ TiLiS2Li Li+ + e-
Rocking chair batteries - intercalation
PHY563 – N. Schneider 38
Li-ion: electrodes = Li+ intercalation compounds
anodecathode
Rocking chair batteries - intercalation
PHY563 – N. Schneider 39http://electronics.howstuffworks.com/everyday-tech/lithium-ion-battery1.htm
Conventions
• Anode: negatively charged electrode
• Cathode: positively charged electrode
Li Battery at equilibrium
• Negative electrode
Li° Li+ + e- or LixC6 e Li+ + e e- + Lix-eC6
• Positive electrode
e Li+ + e e- + LixMOy Lix+eMOy
• In all cases :
o µLi = µLi+ + µe at each electrode
o µLi+ is constant through electrolyte (equilibrium)
o Hence: V = µeanode - µe
cathode = -µLianode + µLi
cathode
• µLi is related to the formation energy of the electrode
o e.g. O2+ Co +Li LiCoO2
o i.e. µLi + µO2 + µCo = DGf ; µLi° = 0
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In this system the electrolyte is « invariant »While electrodes are the « redox » solids
Potential and material properties
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Single-phase systemex: LixTiS2
Two-phase systemex: LixFePO4
Li-technologies – electrode materials
PHY563 – N. Schneider 46
LiMnO2/LiCoO2 : 10% less capacity advantage : cost & green
to achieve higher capacities : design materials in which the metal-redox oxidation state can change reversibly by 2 units :
Mn+2/Mn
Preserving frame work structure Molecular masses similar to 3d metal-layer oxides (ex : LiMnO2 or LiCoO2)
Not W, Mo ou Nb : heavy V-based oxides L3V2O5-Li3V3O8
Cr6+/Cr3+
LiMnO2 : structural instability upon cycling : substitution by Cr : Li1+X Mn0.5Cr0,5O2
Capacity : 190 mAhg-1
Mn : stabilize the layered structureCr : large capacity due to oxidation state that changes from +3 to +6
But Cr : presents major toxicity & pricing issues
Li-S and Li-air batteries
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Challenges on Li-air battery:- avoid undesired
reactions (LiO2, …) : need for electro-catalyst,
- avoid dendriticreplating of Li
- non floodingelectrolyte
- Li anode protection from air
- scrubbing system for the air
Tarascon, cours Collège de France (2011)
Na technology
PHY563 – N. Schneider 51Tarascon, cours Collège de France (2011)
Na vs Li
(+) cost(Na2CO3 0.1€/kg vs. Li2CO3 3.5€/kg)abundant
(-) potential -0.3Vcapacity (rionique)
Na technology
PHY563 – N. Schneider 52Tarascon, cours Collège de France (2011)
• Na/S – high T system
o Large scale batteries
o Mature
o Safety issues
Vegetal alternatives
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Organic material 1
(electroactive with high potential
3 V vs Li+/Li0)
Non-aqueous electrolyteElectrode (+) Electrode (-)
Li++ -
e e
Organic material 2
(electroactive with low potential
0.5 V vs Li+/Li0)
BIOMASS
From P. Poizot, LRCS
ex: rhodizonate(maïs)
• Li batteries:
Invariant electrolyte and redox electrodes
• Other batteries could have redox electrolyte and invariant electrodes
Exemple : concentration Cu cell
Still other case with electrolytes redox and inert electrodes (e.g., graphite) > Redox flow
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Redox electrolytes
Redox flow batteryPower : surface area of the electrodes
Energy : amount of liquid electrolyte(size of storage tanks)
Power and Energy separated
Redox flow batteries
• Reactants are liquid and heldin large tanks high energy-storage capacity
• Key-element = membraneo Separated two solutions +
selective (only 1 ion) or anio(catio)ic (only anion or cation)
o If mix of electrolytestreatment of solutions (cost)
• Different systems: Fe/Cr, V/Br, Zn/Br, VRB (all V-species, lessinterdiffusion issues)
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Redox flow batteries
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Vanadium Redox Batteries (VRB)
o Negative: V2+/V3+ ; positive: V4+/V5+ , acidic sol.
o 4 ions form the same element Less interdiffusion issues
Redox flow batteries
Advantages Disadvantages
Large lifetimePower/Energy are decoupledSeasonal storage possible
Low specific energy and powerHigh costSelf discharge
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Catalysis
• What is a catalyst?
• Which type of catalyst exist?
• Is it relevant?
• Some examples
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Catalysis – fundamental notions
• Catalysis = increase of chemical reaction rate due to the participation of an additional substance (catalyst) : thermodynamics / kinetics
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Ea = activation energy
= transition state
k = A.e-Ea/RT (Arrhenius)
o
oo
Catalyzed reaction : ≠ intermediates/ transition stateslower Ea
o = intermediate
Catalysis – fundamental notions
• Different types of catalysis
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HETEROGENEOUS Cat. and reactants in different phasesHOMOGENEOUS Cat. and reactants in the same phase, usually liquid
(+) Good contact with reactants(+) Ease of characterization/tuning(-) Catalyst needs to be separated after the reaction(-) Difficult catalyst recovery
ENZYMATIC Cat. is an enzyme
(+) Most highly efficient systems(+,-) Highly specific
(+) Little difficulty in separating and recycling the catalyst(-) Lower effective concentration of catalyst
Ni Raney: Ni/Al
Wilkinson cat.: RhCl(PPh3)3
Polyneuridine AldehydeEsterase
catalyst
loading (mol%)
activity (mol.s-1, quantity converted/time, or TOF (turn-over frequency
selectivity ability to yield a particular product
stability TON (turn-over number)
Catalysis – fundamental notions
• Adsorption / physisorption / chimisorptionPhysisorption:
Exothermic (10-40 kJ.mol-1)low / no Eaweak interaction (VdW)f(P), f (specific area)
Chimisorption:exothermic, Qads = Ebond (60-120 kJ.mol-1)High Eastrong interaction (OM overlaping)f(P), f(surface nature, defects, active sites)
- Langmuir model – monolayer- BET (Brunauer, Emmet, Teller) model – multilayers (chimisorbed + physisorbed molecules on top)
Catalysis – fundamental notions
• Catalyst dispersion / active siteso Dispersion = nb accessible atoms / total nb of atoms
o Dispersion can be increased by supported catalysts
o Dispersion can be increased by the use of nanoparticles
Handbook of Heterogeneous Catalysis, Wiley, 2008
Catalysis – fundamental notions
• Supportso Should prevent sintering effects
o Can have acid/base properties bifunctionnal catalysis
o Can allow biphasic systems
o Oxides, Silica, Zeolites (SiAlOxM, M can be a catalyst), graphite, microporous and mesoporous materials (micelles, use of templates)
o Pore size determination: Hg porosimetry, BET
Melero et al, J. Mater. Chem. 2002 12 1664
Silica SiO2
graphite zeolites
SBA-15
Catalysis – fundamental notions
• Accessible sites ≠ active sites : structure-sensitiveo Electronic properties are size-dependent
o Shape may vary during the reaction
o Large particles are not spherical: atoms with ≠ coordinence
74Lin et al, Phys. Rev. Lett. 102, 206801 (2009)
Catalysis – significance and main applications
• Academia
PHY563 – N. Schneider75
Fig. 1 Subject area breakdown of Catalysis Science & Technology's 2014 published articles.
Catalysis – significance and main applications
• Industry90% of industrial processes are catalyzed
(1) Bulk chemicals
- polymerisation (Ziegler-Natta)
- oxydation (nitric/sulfuric acid)
- hydrogenation (NH3 Haber-process, methanol)
- carbonylation (acetic acid, Monsanto-process)
(2) Fine chemicals
- olefin metathesis
- Friedel-Craft
- asymmetric synthesis (pharmaceuticals)
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Catalysis – significance and main applications
(3) Energy processing
CO2 reduction
See PC
Fuel cells
metal catalysts at both anode and cathode to catalyze half-reactions
commercial devices: Pt nanoparticles or Pt alloy supported on C black
« main obstacle for larger fuel cellcommercialisation »
research devices: doped C nanotubes, Ni-Cr, Ni-Al or Ni-O alloys
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Source: D. S. Ginley et al, Fundamentals of materials for energy and environmental sustainability-Cambridge University Press (2012)
Catalysis – significance and main applications
(3) Energy processing
Catalytic converters
(petroleum exhaust)
PHY563 – N. Schneider78Source: Handbook of Heterogeneous Catalysis, Wiley, 2008
Reduction (Rh) : NOx N2
Oxydation (Pt) : CO CO2 , HC CO2 + H2Oλ probe + cordierite support + Al2O3 washcoat + CeO2 O2 storage promoters + Pt + Rh
Catalysis – significance and main applications
(3) Energy processing
Catalytic converters
(petroleum refining)
alkylation, cracking, naphta and steam reforming (HC syn-gas)
PHY563 – N. Schneider79
( CO, H2 )
( CO, H2 )
( H2O, CH4 )
steam reforming
Water-gas-shiftH2O + CO CO2 + H2
Adjusted syn-gas, H2/CO=2
syn-gas, H2/CO=0.7
Hydrocarbons + H2OFischer-Tropsch
Catalysis – significance and main applications
(3) Energy processing
Fischer-Tropsch
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History
1923 : patent from Franz Fischer and Hans Tropsch(Kaiser-Wilhelm-Institut für Kohlenforschung, Mülheiman der Ruhr)
WWII : ersatz fuel (90% plane, 25% automobile)
50’s : South Africa
70’s : Regain of interest due to oil price increase
currently : Sasol, PetroSA, Linc Energy, Shell
Catalysis – significance and main applications
(3) Energy processing
Fischer-Tropsch
PHY563 – N. Schneider81
Sasol-Qatar Petroleum Oryx plant
Catalysis – significance and main applications
(3) Energy processing
Biomass
conversion
PHY563 – N. Schneider83
biomass
SyngasSynthetical gas, {CO + H2}
MethanolCH3OH
Cat. Cu/ZnO440°C, 50 atm
GasificationControlled amount of O2
Hydrocarbon chainsCnH2n+2
Fischer-Tropf process
Fischer-Tropf processtypically catalyzed by Co, FeT 300°C
challenges: - control n value- catalyst deactivation- …