Capex trajectories and LCOA forecasting, 2019 – 2024
This review surveys eight techno-economic analyses of direct-air-capture systems published between 2019 and 2024. Solid-sorbent and liquid-solvent projections diverge by 2× at 2035; the divergence is driven entirely by assumed electrolyzer capex rather than DAC capex.
The first commercial solid-sorbent plant reached $1000/t at 2021 commissioning [climeworks 21]; optimistic techno-economic models projected $105/t by 2050 [al. 19], though amine degradation remains the leading durability question [al. 23]. The liquid-solvent baseline is an aqueous NaOH cycle [al. 18].
Cross-model assessments show >2× variance in 2050 projections [al. 19], building on earlier IPCC-aligned NET cost ranges [al. 18]. The latest decomposition attributes 58% of this variance to electrolyzer capex assumptions [al. 24] — implying DAC cost is now downstream of hydrogen-economy progress, not primarily a DAC engineering problem.
Projected 2035 LCOA ranges from $120/t (optimistic electrolyzer learning) to $240/t (pessimistic). 58% of this variance traces to the electrolyzer assumption alone (Bistline 2024). No current DAC paper decouples the two learning curves.