Membrane-Free Electrochemical Reactor

Gravity-Assisted Product Self-Separation (GAPS) Reactor

A breakthrough in electrochemical oxygen removal that leverages Stokes flow and buoyancy-driven bubble dynamics to achieve 95% product self-separation — eliminating the need for costly ion-exchange membranes.

Li, P., Tang, X., Zhou, X., et al. "A membrane-free electrochemical reactor for efficient oxygen removal via gravity-assisted product self-separation."

Nature Communications, 16, 4309 (2025). DOI: 10.1038/s41467-025-59506-7

University of Science and Technology of China · Hefei Hualing Co., Ltd · Anhui Entropy Carnot Energy Technology Co., Ltd

Key Results

Product Self-Separation

95%

O₂ bubbles self-separate via buoyancy without membranes

Operational Lifespan

10 years

Integrative GDE with 30× greater stability than carbon paper

Fresh-Keeping Improvement

3.4×

Two-cell system in household refrigerator

Cost Efficiency

22.6×

O₂ removal per unit cost vs. ion-exchange membrane reactors

Gravity-Driven O₂ Separation

The GAPS Reactor exploits the density differences among three phases — the electrode (high density), the liquid electrolyte (medium density), and the gas phase (low density) — to achieve spontaneous, buoyancy-driven O₂ migration.

When O₂ bubbles form at the anode through the oxygen evolution reaction (OER), they immediately enter the bulk electrolyte. The inherent density gradient creates a self-organizing "O₂ ladder" that allows bubbles to naturally ascend and exit the liquid surface without external pumping or membrane separation.

The cathode, positioned at the reactor's base, performs the oxygen reduction reaction (ORR), selectively removing O₂ from the storage environment. A large-area open cathode design overcomes mass transfer limitations that would otherwise result from the absence of a gas-liquid circulation system.

Re = ρ_l · v_b · (2r) / μ_l

Where ρ_l is liquid density, v_b is bubble rising speed, 2r is bubble diameter, and μ_l is liquid viscosity.

v_b = 2r²(ρ_l − ρ_g)g / 9μ_l

Using 20% K₂CO₃ electrolyte: v_b = 0.175–0.486 m/s for r = 0.3–0.5 mm. Bubble rise time for h = 0.05 m is 0.10–0.28 s.

Cathodic ORRO₂(internal) + 2H₂O + 4e⁻ → 4OH⁻
Anodic OER4OH⁻ − 4e⁻ → O₂(external) + 2H₂O
OverallO₂(internal) → O₂(external)

Integrative Gas Diffusion Electrode

Conductivity

85.5%

relative to conventional carbon paper

Gas Permeability

80.2%

relative to conventional carbon paper

Mechanical Strength

2.2×

higher than carbon paper GDE

The integrative GDE addresses the critical limitations of traditional carbon paper-based electrodes. By thoroughly mixing carbon spheres with a high loading of PTFE and sintering the mixture, the resulting electrode achieves uniform PTFE distribution — eliminating the uneven distribution that undermines the electrochemical stability of conventional designs. The result is an electrode with 30× greater operational stability, enabling the 10-year lifespan required for consumer applications.