Abstract
Using mixed microbial culture (MMC) to produce polyhydroxyalkanoates (PHA) from waste streams is cost-effective and sustainable. However, low biomass and PHA accumulation under certain conditions limit PHA yield. This study developed a one-pot synthesis process for both biomass and intracellular PHA content of MMC under salinity and high organic load, without nitrogen limitation, ensuring long-term operation and high PHA yield. After 18hours of cultivation with the substrate chemical oxygen demand (COD) of 20000±100mg/L, 20% inoculation amount, 0.8% substrate salinity and initial pH 8.0, the mixed liquor volatile suspended solids (MLVSS) increased from 0.69 to 6.64g/L, achieving a PHA content of 0.56±0.01g PHA/g VSS and volumetric productivity of 0.21±0.01g/(L•h). Real food waste fermentation leachate (FWFL) verification showed a higher MLVSS (7.10g/L) but a 10% reduced PHA content and productivity. Microbial analysis revealed that PHA-producers dominated throughout the 18-hour cultivation, with the continuous high relative abundance of phaC. This process simultaneously boosted biomass and PHA accumulation, enhanced the PHA yield and offered industrial potential.
| Original language | English |
|---|---|
| Article number | 117293 |
| Journal | Journal of Environmental Chemical Engineering |
| Volume | 13 |
| Issue number | 4 |
| DOIs | |
| State | Published - Aug 2025 |
Keywords
- ADF aerobic dynamic feeding
- Abbreviations FWFL food waste fermentation leachate
- HRT hydraulic retention time h
- PHAintracellular PHA concentration of bacteria at the beginning time, g COD/L
- PHAintracellular PHA concentration of bacteria at the sampling time, g COD/L
- PPHA accumulation capability, g PHA/g VSS
- PPHA volumetric productivity g/L•h
- Pbiomass volumetric productivity g/L•h
- QPHA production rate, g COD/g X/h
- Qspecific substrate uptake rate, g COD/g X/h
- SRT sludge retention time d
- SVI sludge volume index mL/g
- Sthe substrate concentration at the beginning time g COD/L
- Sthe substrate concentration at the sampling time g COD/L
- Xbiomass excluding polymers PHA at the beginning time g /L
- Xbiomass excluding polymers PHA at the sampling time g/L
- Ybiomass growth yield on substrate g COD/g COD
- Yyield of PHA production on substrate g COD/g COD
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