Received:
09 April 2026
Revised:
11 July 2026 Accepted:
22 July 2026
Published online:
14 September 2026
Engineering in Life Sciences26(9),
Article number: e011 (2026) | Cite this article
Abstract
Electrobiotechnology is increasingly recognized as a key platform technology for sustainable production processes, as it allows direct coupling of renewable electricity with biocatalysis, driving selective chemical transformations. One remaining challenge is the development of suitable reactors fulfilling both electrochemical and biocatalysis requirements. Conventional setups, often used as proof-of-concept, often represent negative examples regarding scalability and industrial relevance. Scalable, electrified bioreactors are needed for screening purposes and for large-scale bioproduction. This study presents a small-scale, electrified bioreactor (V = 20 mL) that can facilitate a variety of electrochemical conditions and bioprocess modes. Two reactor configurations based on the commercial Pioreactor® were established: a two-electrode one-chamber system for electro-autotrophic growth via in situ hydrogen production, and a three-electrode two-chamber system for anodic respiration via mediated electron transfer. Additionally, it was used for electrochemical adaptive laboratory evolution (eALE). Under turbidostatic electro-autotrophic conditions with gradually increasing sodium sulphate concentrations, an osmo-tolerant strain was obtained within 10 d. The adapted variant exhibited improved growth at 300 mM sodium sulphate compared to the parental strain, including reduced lag-phase and a higher final optical density. Cupriavidus necator was used as a model organism. Overall, the results suggest that the system establishes a viable connection between microtiter plates and established liter-scale bioreactor operations.
Supplementary Fig. S1
Batch cultivation in the electrified Pioreactor®C. necator ΔPHB was cultivated in the electrified Pioreactor® under
electro-autotrophic conditions in minimal medium at 30 °C and 500 rpm for 7 days.
Supplementary Fig. S2
Calculated Na2SO4 concentration in mM during the continuous eALE process over time.
Supplementary Table S1
Maximal specific growth rate of C. necator ΔPHB and the adePio variant during hours 6–20 of heterotrophic growth with different concentrations of sodium sulphate and statistical analysis
via Welch-t-test (significant if p < 0.05).