Algae PHA / PHB pipeline
Photobioreactor cultivation through solvent-free PHA extraction to melt-spun biopolymer fibre. Every stage is a deterministic mass balance; change a setpoint and the twin recomputes.
Fibre per cycle
419.98 kg
7299.68 kg / yr
CO₂ fixed
3251.18 kg
1.83 kg CO₂ / kg DW
Energy intensity
5889.98 kWh
11.5 kWh / kg polymer
Gross margin
$-6272.16
revenue $3527.84 − opex $9800
Tenacity (model)
12.54 cN/dtex
PHB melt-spun estimate
Cycles / year
17.38
21-day cycle
Mass balance
- 01Photobioreactor cultivation1,890 kg DW
18 g/m²/d × 5000 m² × 21 d
- 02Harvest & dewatering1,776.6 kg DW
DAF + centrifuge, 6% loss
- 03PHA accumulation746.17 kg
42% of dry weight
- 04Solvent-free extraction582.01 kg crude
78% recovery
- 05Purification / pelletising512.17 kg PHB
88% conversion
- 06Melt spinning → fibre419.98 kg fibre
82% spinning yield
Model notes
- Biomass = area × areal productivity × cycle days, minus 6% harvest loss (DAF + centrifugation).
- Carbon fixation assumed at 1.83 kg CO₂ per kg dry biomass (Redfield-derived stoichiometry).
- Tenacity proxy: 0.18·PHA% + 0.09·spinning yield − 2.4, valid for melt-spun PHB monofilament.