Sodium-Sulfur Battery: Molten Electrode Cell

Cell Operation

Current rate 0.20 C

Cell temperature 320 °C

Cell State

SOC 100%S₈ regime

Terminal voltage

2.076 V

Current density

0 mA/cm²

Na⁺ ionic flux

0 ions/s

β″-alumina R_int

— Ω·cm²

How it works

A NaS cell holds molten sodium (m.p. 98 °C) and molten sulfur/sodium‑polysulfide (m.p. 115 °C) apart with a beta‑alumina solid electrolyte (BASE) tube that conducts only Na⁺ ions — everything runs above ~300 °C so both electrodes stay liquid. Discharge reaction:

2 Na + x S  →  Na₂S_x     (5 ≲ x ≲ 8, x decreasing as discharge proceeds)

The open-circuit voltage is set by the two-phase liquid regions the sulfur passes through, giving the battery's signature double plateau:

V_ocv ≈ 2.076 V   while S₈-rich liquid + Na₂S₃ coexist (SOC ≳ 24%)
V_ocv ≈ 1.78  V   once composition crosses into the Na₂S₃–Na₂S₂ region (SOC ≲ 24%)

Terminal voltage subtracts an internal-resistance drop, V = V_ocv − I·R_int. R_int comes from the Na⁺ conductivity of the ceramic, which follows an Arrhenius law — hotter cells conduct better and lose less voltage under load:

σ(T) = σ₀ · exp(−E_a / k_B T),   R_int ∝ 1/σ(T)

Discharge / Charge / Hold — sets the direction ions cross the electrolyte; Na⁺ leaves the anode pool (its level visibly drops) and migrates outward into the sulfur cathode on discharge, and reverses on charge.
Current rate — the C-rate driving Na⁺ flux; higher current drains state-of-charge faster and produces a larger I·R_int voltage sag.
Cell temperature — raises ionic conductivity of the beta-alumina, shrinking R_int and the voltage sag for the same current.

Real cells (e.g. NGK's NAS units) run this exact chemistry at grid scale for multi-hour storage, prized for high round-trip efficiency and no self-discharge — the tradeoff is the standing 300+ °C operating temperature simulated here.

Molten sodium (anode) β″-alumina electrolyte Sulfur / polysulfide (cathode) Na⁺ ion

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