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Battery Materials

Which chemical compounds actually go into batteries — not just "lithium" or "cobalt", but the specific precursors (Li₂CO₃, CoSO₄, NiSO₄), cathode chemistries (NMC, LFP, NCA), and non-metal components (graphite, phosphorus). Covers Li-ion, Lead-acid, NiMH, and flow batteries. Each material links to the underlying metal page in the Hub where available. Primary sources below.

Dominant chemistry
Lithium-ion
EV, grid storage, portable electronics, power tools
Oldest chemistry
Lead-acid
Automotive starter batteries, UPS, backup power
Hybrid vehicles
NiMH
Hybrid vehicles, power tools, low-cost electronics
Grid-scale storage
Vanadium flow
Long-duration (4–12 h) stationary storage

Lithium-ion Battery Materials

The dominant battery chemistry today. Cathode composition varies (NMC, NCA, LFP, LCO, LMO), but anode is almost always graphite with small additions of silicon. Electrolyte is a lithium salt dissolved in organic solvents.

Material Chemical form Role Used in
Lithium Li₂CO₃ lithium carbonate
LiOH·H₂O lithium hydroxide monohydrate
LiPF₆ in electrolyte salt
cathode precursorelectrolyte All Li-ion (NMC, NCA, LFP, LCO, LMO)
Cobalt CoSO₄·7H₂O cobalt sulfate heptahydrate cathode precursor NMC, NCA, LCO
Nickel NiSO₄·6H₂O nickel sulfate hexahydrate (Class 1 Ni) cathode precursor NMC, NCA (high-Ni cathodes: NMC 811, 622)
Manganese MnSO₄·H₂O manganese sulfate monohydrate cathode precursor NMC, LMO, Na-ion (emerging)
Aluminium Al metal (0.3–6% doping in NCA)
Al foil (cathode current collector)
cathode dopantcurrent collector NCA (LiNi₀.₈Co₀.₁₅Al₀.₀₅O₂), all Li-ion (foil)
Copper Cu high-purity foil (6–12 μm) anode current collector All Li-ion (anode side)
Iron LiFePO₄ (LFP, iron phosphate cathode) cathode LFP — fastest-growing chemistry (China EV, grid storage)
Phosphorus non-metal LiFePO₄ as phosphate group
LiPF₆ as hexafluorophosphate (electrolyte salt)
cathode (LFP)electrolyte LFP cathodes, all Li-ion electrolyte
Graphite non-metal C natural or synthetic graphite (spherical, coated) anode (active material) All Li-ion (>90% by mass of the anode)
Silicon non-metal SiO silicon monoxide, Si metallic (nanostructured) anode additive High-energy Li-ion (5–15% Si blend with graphite)
Fluorine non-metal LiPF₆, PVDF binder electrolyte saltbinder All Li-ion
Note on precursor vs battery grade: Cobalt and nickel sulfates must be "battery grade" — far higher purity (typically ≥99.9%, with strict trace-metal limits) than chemical-grade commodity sulfate. This is why Class 1 nickel (refined cathode, briquettes, powder) commands a premium over Class 2 (ferronickel, nickel pig iron).

Li₂CO₃ vs LiOH — which cathode needs which

Both are lithium salts used as cathode precursors. The choice is dictated by the target cathode chemistry: high-nickel cathodes (NMC 811, NCA) need lithium hydroxide because it reacts at lower temperatures and avoids nickel oxidation. Lower-nickel and LFP cathodes can use cheaper lithium carbonate.

Lithium carbonate
Li₂CO₃
  • Li content~18.8% by mass
  • Calcination~900 °C (higher)
  • CathodesLFP, LCO, LMO, NMC 111 / 532
  • SolubilityLow in water (~13 g/L)
  • SourceBrine (direct), spodumene (via sulfate)
  • Price tierLower (~30% cheaper per kg Li)
  • StorageEasier — not hygroscopic, not caustic
Lithium hydroxide
LiOH·H₂O
  • Li content~16.5% by mass (monohydrate)
  • Calcination~700 °C (lower — key for high-Ni)
  • CathodesNMC 622 / 811 / 9.5.5, NCA, LMFP
  • SolubilityHigh (~128 g/L)
  • SourceSpodumene (direct), brine (via Li₂CO₃ conversion)
  • Price tierHigher (premium for high-Ni chemistry)
  • StorageHygroscopic, caustic — stricter handling
LME contract: The LME lists Lithium Hydroxide CIF (Fastmarkets) — not Li₂CO₃ — because LiOH is the dominant feedstock for EV-grade high-Ni cathodes, which drive the marginal ton of lithium demand. (LME lithium hydroxide contract specs)

Nickel Class 1 vs Class 2 — why it matters for batteries

"Nickel" as a commodity is not one product. The LME-deliverable cathode, briquettes, and powder (Class 1) are battery-suitable after dissolution to sulfate. Nickel pig iron, ferronickel, and matte (Class 2) go almost entirely to stainless steel. The distinction drives a persistent price premium.

Class 1 nickel
≥99.8% Ni
  • FormsCathode (full plate, cut), briquettes, powder, pellets
  • RouteSulfide ore → concentrate → smelt → refine (electrowinning or carbonyl)
  • End usePlating, specialty alloys, superalloys, batteries (dissolved to NiSO₄)
  • Battery pathDissolve in H₂SO₄ → crystallise NiSO₄·6H₂O (battery-grade)
  • LME deliverable?Yes (LME cathode, briquettes, powder)
  • Major producersNorilsk, Vale, BHP, Sumitomo, Jinchuan
Class 2 nickel
~1.5–38% Ni
  • FormsFerronickel (20–38% Ni), Nickel Pig Iron (4–15% Ni), matte (~75%), MHP, MSP
  • RouteLaterite ore → rotary kiln / electric furnace (RKEF) or HPAL
  • End useStainless steel (~95% of Class 2)
  • Battery pathMHP/MSP (mixed hydroxide / sulfide precipitate) → leach → NiSO₄ (emerging HPAL route, Indonesia)
  • LME deliverable?No (stainless-grade only)
  • Major producersTsingshan (Indonesia), PT Vale Indonesia, Eramet, Antam
The Indonesia shift: Historically batteries used Class 1 nickel (sulfide ore). Tsingshan's 2021 breakthrough converting HPAL laterite intermediates (MHP) into battery-grade sulfate collapsed the Class 1/Class 2 wall and pushed Indonesian laterite supply into the EV supply chain. This is the single biggest structural shift in the nickel market this decade. (USGS MCS 2026 — Nickel)

Lead-acid Batteries

The oldest rechargeable chemistry, still dominant in automotive starter batteries, uninterruptible power supplies, and backup power. Global lead demand is roughly 80% driven by this chemistry.

Material Chemical form Role Used in
Lead Pb metallic (grid, negative plate)
PbO₂ lead dioxide (positive plate)
PbSO₄ lead sulfate (discharged state)
positive platenegative plate SLI (starter/lighting/ignition), UPS, traction, stationary
Sulfuric acid non-metal H₂SO₄ 30–40% in water electrolyte All lead-acid batteries
Antimony / Calcium Sb ~2% in Pb alloy (older), Ca in maintenance-free alloying element (grid) Pb-Sb (flooded), Pb-Ca (VRLA/AGM)

Nickel-metal Hydride (NiMH)

Dominant in hybrid vehicles, power tools, and consumer electronics before Li-ion took over. Still used where cost matters more than energy density.

MaterialChemical formRoleUsed in
Nickel NiOOH / Ni(OH)₂ positive electrode All NiMH
Rare Earths LaNi₅ / AB₅ alloys (La, Ce, Pr, Nd + Ni, Co, Mn) negative electrode (hydrogen storage) Hybrid vehicle batteries, consumer NiMH
Potassium non-metal (alkali) KOH potassium hydroxide, 30% aqueous electrolyte All NiMH and NiCd

Flow Batteries (grid-scale storage)

Long-duration stationary storage (4–12 hour discharge). Energy is stored in liquid electrolytes in external tanks, not solid electrodes — so power and energy scale independently. Vanadium redox (VRFB) is the dominant commercial chemistry; Zn-Br and Fe-flow are emerging.

MaterialChemical formRoleUsed in
Vanadium VOSO₄ vanadyl sulfate
VO₂⁺ (V⁵⁺, charged — positive half-cell)
VO²⁺ (V⁴⁺, discharged)
V³⁺ (discharged — negative half-cell)
V²⁺ (charged)
both half-cells (single-element redox) Vanadium redox flow batteries (VRFB)
Zinc Zn metal, ZnBr₂ bromide, Zn(OH)₄²⁻ zincate negative half-cell Zn-Br, Zn-Fe, Zn-air flow batteries
Iron Fe²⁺/Fe³⁺ in citrate or chloride complex both half-cells (Fe-Fe flow) or one (Zn-Fe) All-iron flow (ESS Inc.), Zn-Fe (ViZn)
Bromine non-metal (halogen) Br₂ / Br⁻, polybromide complexes positive half-cell Zn-Br flow (Redflow, Primus Power)
Sulfuric acid non-metal H₂SO₄ 1.5–3 M electrolyte solvent All VRFB
Why vanadium works uniquely well: Vanadium has four stable oxidation states in aqueous solution (V²⁺, V³⁺, V⁴⁺, V⁵⁺), so a single element can serve both half-cells. This eliminates cross-contamination problems that plague two-element redox couples — if membrane crossover occurs, the electrolyte can be fully recovered by rebalancing. Expected service life 20+ years with minimal degradation. Main drawbacks: low energy density (~25–35 Wh/L vs. ~250 Wh/L Li-ion), vanadium price volatility, and the cost of large electrolyte tanks. (USGS MCS 2026 — Vanadium; IEA — Batteries and Secure Energy Transitions 2024)
Notable projects: The 100 MW / 400 MWh Dalian VRFB in China (Rongke Power, phase 1 commissioned 2022) is the world's largest flow battery by capacity. Hubei Zaoyang 100 MW / 500 MWh and Xinjiang Urumqi 100 MW / 500 MWh follow. Western deployments are smaller: Invinity's EnerVenue and Sumitomo Electric projects in the US and Japan are in the 10–50 MWh range. (IEA Batteries Report)

Emerging chemistries (Na-ion and beyond)

Sodium-ion batteries are now commercially produced by CATL, BYD, and others. They use abundant materials (Na replaces Li) and are cheaper, with lower energy density. Typical cathode is a Prussian-blue analog or layered oxide.

MaterialChemical formRoleUsed in
Sodium alkali metal Na₃V₂(PO₄)₃, NaNi₁/₃Mn₁/₃Fe₁/₃O₂, Prussian-blue Na₂MnFe(CN)₆ cathode active material Na-ion (stationary storage, low-end EVs)
Hard carbon non-metal C non-graphitizable carbon anode (Na-ion cannot intercalate graphite efficiently) Na-ion

From Ore to Battery — typical concentrations along the chain

Battery metals start in the ground at very low concentrations. Mining, beneficiation, smelting, and refining progressively upgrade the material to the purity required by the cathode or anode plant. Numbers below are typical ranges from primary sources — individual deposits vary widely.

Lithium — from spodumene pegmatite
Run-of-mine ore
Spodumene pegmatite
1.0–2.0% Li₂O
Concentrate (flotation)
Spodumene concentrate
6.0–7.0% Li₂O
Intermediate salt
Li₂SO₄ (after acid roast/leach)
Battery precursor
Li₂CO₃ or LiOH·H₂O
≥99.5% Li₂CO₃
Lithium — from brine (Chile, Argentina)
Raw brine
Salar (Atacama)
200–1,500 ppm Li
Concentrated brine
After solar evaporation (12–18 mo)
~6% Li (~60,000 ppm)
Battery precursor
Li₂CO₃ (direct precipitation)
≥99.5%
Nickel — sulfide route (Class 1)
Run-of-mine ore
Pentlandite / pyrrhotite
1.5–3% Ni
Concentrate (flotation)
Nickel sulfide concentrate
10–20% Ni
Matte (smelt)
Ni₃S₂ matte
~75% Ni
Refined (LME)
Cathode / briquettes
≥99.8% Ni
Battery precursor
NiSO₄·6H₂O
~22% Ni
Nickel — laterite route (Class 2 → batteries, HPAL)
Run-of-mine ore
Limonite / saprolite (laterite)
0.8–2.5% Ni
HPAL leachate
Ni-Co pregnant liquor
Intermediate
MHP (Mixed Hydroxide Precipitate)
~35–40% Ni
Battery precursor
NiSO₄·6H₂O (re-leach)
~22% Ni
Cobalt — DRC copper-cobalt belt (dominant source)
Run-of-mine ore
Heterogenite (oxide) / carrollite (sulfide)
0.3–1.0% Co (DRC)
Concentrate
Cu-Co concentrate (co-product)
Intermediate
Cobalt hydroxide (from SX-EW tailings)
~30–40% Co
Battery precursor
CoSO₄·7H₂O
~21% Co
Copper — porphyry (dominant source)
Run-of-mine ore
Porphyry (chalcopyrite)
0.3–1.0% Cu
Concentrate (flotation)
Copper concentrate
~25–30% Cu
Refined (LME)
Cathode, Grade A
≥99.9935% Cu
Battery form
Rolled Cu foil, 6–12 μm
≥99.99% Cu
Vanadium — titaniferous magnetite (85% of supply)
Run-of-mine ore
Titaniferous magnetite
0.3–2.0% V₂O₅
Steel slag co-product
Vanadium-bearing slag (BOF)
~0.9% V₂O₅
Intermediate
V₂O₅ flake (salt roast / leach)
≥98% V₂O₅
Flow-battery form
VOSO₄ electrolyte (1.6 M V in H₂SO₄)
Graphite — natural flake route (anode)
Run-of-mine ore
Graphitic schist
5–20% C
Concentrate (flotation)
Flake graphite concentrate
94–98% C
Purification
Thermal or acid-leach
≥99.95% C (battery grade)
Anode form
Spheroidised, coated (CSPG)
≥99.95% C
Concentration factors (intuition): Lithium from spodumene → Li₂CO₃ is a ~50× upgrade. Copper from porphyry ore → cathode is ~333×. Cobalt from African copperbelt ore → CoSO₄ is ~50×. Vanadium from titanomagnetite → V₂O₅ is ~100×. Each step in the chain carries energy, reagent, waste, and royalty costs — which is why "raw tonnes mined" looks nothing like "tonnes delivered to the cathode plant."

Sources

This page is a reference, not investment advice. Chemistry details are simplified for readability; commercial formulations vary by manufacturer. Concentrations are typical industry ranges — individual deposits and refineries vary. More materials (Li-S, solid-state, Zn-air) will be added in future revisions.