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Projects, one carbon-utilization stack

Flagship projects that, together, span the full path from catalyst surface to plant-scale economics. Each is summarized with its problem, approach, results, and outputs.

§ 01 active

Tandem Gas-Diffusion Electrodes for C2+

A structured Cu–Ag bilayer that decouples CO generation from C–C coupling.

The problem

Copper is the only metal that couples CO₂ to multicarbon products, but it wastes current on hydrogen and CO.

The approach

Pair a CO-generating silver layer with a coupling-optimized copper layer across a tuned gas-diffusion electrode.

Key results

74% C2+ Faradaic efficiency at 300 mA cm⁻², sustained over 200 hours.

74%
C2+ Faradaic efficiency
300
mA cm⁻²
200 h
stable operation
Preparing copper catalyst inks for tandem gas-diffusion electrodes
Electron microscopy of a flood-resistant membrane-electrode assembly microstructure
§ 02 active

Flood-Resistant Membrane-Electrode Assemblies

Hydrophobic-gradient MEAs that run for weeks without flooding.

The problem

Gas-diffusion electrodes flood as salts precipitate, collapsing performance within hours.

The approach

Engineer a wettability gradient through the catalyst and transport layers to expel liquid water.

Key results

1000 hours of stable CO₂ electrolysis with less than 10% performance loss.

1000 h
continuous run
<10%
performance loss
200
mA cm⁻²
§ 03 wrapping

The Ethylene Cost Floor

A techno-economic model for when electrochemical ethylene beats cracking.

The problem

It is unclear which performance targets actually make CO₂-to-ethylene economical.

The approach

Build a bottom-up cost model coupling electricity price, selectivity, and durability.

Key results

Identified the electricity-price and selectivity frontier where electrochemical ethylene is cost-competitive.

$0.03
kWh⁻¹ threshold
70%
FE target
durability need
Techno-economic analysis charts for CO₂-to-ethylene electrolysis