Integrated artificial photosynthesis and microbial bioprocessing systems for solar biofuel and bioproduct production

Abstract Coupling abiotic solar capture with microbial biosynthesis integrated artificial photosynthesis–microbial bioprocessing (IAP-MB) could convert sunlight, water and CO 2 into fuels and polymers at areal efficiencies well above those of crops, which typically remain below 1%. Here we critically review three architectures decoupled photovoltaic–electrolysis/fermentation (A), electrode-attached biofilms (B) and photosensitised cells (C) and combine the literature with transparent screening calculations. A cascade analysis bounds the solar-to-chemical efficiency of Architecture A at 4.0–10.9% (base case 7.2%) and identifies electrolysis and bioconversion as the main leverage points. Substrate-inhibited uptake kinetics (Andrews model) imply an unstable operating branch above the optimum carrier concentration (9.8 mM for the constants used), so unmanaged supply–demand mismatch causes runaway accumulation; in simulation, a PI controller with back-calculation anti-windup reduced the peak formate concentration from 207 to 48 mM relative to an unprotected PI loop. Using the authors’ preliminary plant model (10,000 t PHB yr − 1 ), recomputed levelised costs are US$2.19 kg − 1 (A) and US$3.23 kg − 1 (B), dominated by discount rate and operating cost, and photoelectrode lifetimes near one year add roughly US$0.8 kg − 1 to B. Stoichiometrically consistent life-cycle accounting shows that the climate benefit of PHB routes hinges on the biogenic carbon credit (2.04 kg CO 2 per kg PHB): burdens alone are 1.80 (A) and 3.10 (B) kg CO 2 -eq kg − 1 , versus 1.98 for polypropylene. A research roadmap and reporting recommendations close to the paper.

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Publication Details

Journal
Research Square
Published
2026-11-09
DOI
https://doi.org/10.21203/rs.3.rs-11392066/v1
Primary Topic
Microbial Fuel Cells and Bioremediation
Type
preprint
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preprint

Integrated artificial photosynthesis and microbial bioprocessing systems for solar biofuel and bioproduct production

Bandana Ojha, Devesh Ojha
Research Square
Microbial Fuel Cells and Bioremediation
preprint

Integrated artificial photosynthesis and microbial bioprocessing systems for solar biofuel and bioproduct production

Bandana Ojha, Devesh Ojha
preprint en

Abstract

Abstract Coupling abiotic solar capture with microbial biosynthesis integrated artificial photosynthesis–microbial bioprocessing (IAP-MB) could convert sunlight, water and CO 2 into fuels and polymers at areal efficiencies well above those of crops, which typically remain below 1%. Here we critically review three architectures decoupled photovoltaic–electrolysis/fermentation (A), electrode-attached biofilms (B) and photosensitised cells (C) and combine the literature with transparent screening calculations. A cascade analysis bounds the solar-to-chemical efficiency of Architecture A at 4.0–10.9% (base case 7.2%) and identifies electrolysis and bioconversion as the main leverage points. Substrate-inhibited uptake kinetics (Andrews model) imply an unstable operating branch above the optimum carrier concentration (9.8 mM for the constants used), so unmanaged supply–demand mismatch causes runaway accumulation; in simulation, a PI controller with back-calculation anti-windup reduced the peak formate concentration from 207 to 48 mM relative to an unprotected PI loop. Using the authors’ preliminary plant model (10,000 t PHB yr − 1 ), recomputed levelised costs are US$2.19 kg − 1 (A) and US$3.23 kg − 1 (B), dominated by discount rate and operating cost, and photoelectrode lifetimes near one year add roughly US$0.8 kg − 1 to B. Stoichiometrically consistent life-cycle accounting shows that the climate benefit of PHB routes hinges on the biogenic carbon credit (2.04 kg CO 2 per kg PHB): burdens alone are 1.80 (A) and 3.10 (B) kg CO 2 -eq kg − 1 , versus 1.98 for polypropylene. A research roadmap and reporting recommendations close to the paper.

Research Square
Amity University (IN)
Microbial Fuel Cells and Bioremediation
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